CN115594545A - Method for producing Gly-containing water-soluble fertilizer - Google Patents
Method for producing Gly-containing water-soluble fertilizer Download PDFInfo
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- CN115594545A CN115594545A CN202211424128.1A CN202211424128A CN115594545A CN 115594545 A CN115594545 A CN 115594545A CN 202211424128 A CN202211424128 A CN 202211424128A CN 115594545 A CN115594545 A CN 115594545A
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 44
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 19
- DHMQDGOQFOQNFH-UHFFFAOYSA-N Glycine Chemical compound NCC(O)=O DHMQDGOQFOQNFH-UHFFFAOYSA-N 0.000 claims abstract description 175
- 239000004471 Glycine Substances 0.000 claims abstract description 74
- -1 compound amino acid Chemical class 0.000 claims abstract description 43
- 238000002156 mixing Methods 0.000 claims abstract description 22
- 238000000034 method Methods 0.000 claims abstract description 21
- 239000011573 trace mineral Substances 0.000 claims abstract description 21
- 235000013619 trace mineral Nutrition 0.000 claims abstract description 21
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000011575 calcium Substances 0.000 claims abstract description 19
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 19
- 229940038879 chelated zinc Drugs 0.000 claims abstract description 16
- ZHJGWYRLJUCMRT-UHFFFAOYSA-N 5-[6-[(4-methylpiperazin-1-yl)methyl]benzimidazol-1-yl]-3-[1-[2-(trifluoromethyl)phenyl]ethoxy]thiophene-2-carboxamide Chemical compound C=1C=CC=C(C(F)(F)F)C=1C(C)OC(=C(S1)C(N)=O)C=C1N(C1=C2)C=NC1=CC=C2CN1CCN(C)CC1 ZHJGWYRLJUCMRT-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000000909 electrodialysis Methods 0.000 claims abstract description 7
- RZLVQBNCHSJZPX-UHFFFAOYSA-L zinc sulfate heptahydrate Chemical compound O.O.O.O.O.O.O.[Zn+2].[O-]S([O-])(=O)=O RZLVQBNCHSJZPX-UHFFFAOYSA-L 0.000 claims abstract description 5
- 239000011701 zinc Substances 0.000 claims abstract description 3
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 3
- 239000010413 mother solution Substances 0.000 claims abstract 2
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 75
- 239000012452 mother liquor Substances 0.000 claims description 60
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 48
- 235000001014 amino acid Nutrition 0.000 claims description 45
- 238000003756 stirring Methods 0.000 claims description 45
- 239000013078 crystal Substances 0.000 claims description 37
- 239000000243 solution Substances 0.000 claims description 36
- 238000006243 chemical reaction Methods 0.000 claims description 35
- 239000008367 deionised water Substances 0.000 claims description 34
- 229910021641 deionized water Inorganic materials 0.000 claims description 34
- 239000000725 suspension Substances 0.000 claims description 27
- MFUVDXOKPBAHMC-UHFFFAOYSA-N magnesium;dinitrate;hexahydrate Chemical compound O.O.O.O.O.O.[Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MFUVDXOKPBAHMC-UHFFFAOYSA-N 0.000 claims description 22
- 239000000203 mixture Substances 0.000 claims description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 12
- 238000005406 washing Methods 0.000 claims description 11
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 10
- 239000007810 chemical reaction solvent Substances 0.000 claims description 10
- FOCAUTSVDIKZOP-UHFFFAOYSA-N chloroacetic acid Chemical compound OC(=O)CCl FOCAUTSVDIKZOP-UHFFFAOYSA-N 0.000 claims description 10
- 229940106681 chloroacetic acid Drugs 0.000 claims description 10
- VKYKSIONXSXAKP-UHFFFAOYSA-N hexamethylenetetramine Chemical compound C1N(C2)CN3CN1CN2C3 VKYKSIONXSXAKP-UHFFFAOYSA-N 0.000 claims description 10
- 239000012535 impurity Substances 0.000 claims description 10
- 238000010438 heat treatment Methods 0.000 claims description 8
- 238000000926 separation method Methods 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 6
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 5
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 5
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 claims description 5
- QNAYBMKLOCPYGJ-REOHCLBHSA-N L-alanine Chemical compound C[C@H](N)C(O)=O QNAYBMKLOCPYGJ-REOHCLBHSA-N 0.000 claims description 5
- COLNVLDHVKWLRT-QMMMGPOBSA-N L-phenylalanine Chemical compound OC(=O)[C@@H](N)CC1=CC=CC=C1 COLNVLDHVKWLRT-QMMMGPOBSA-N 0.000 claims description 5
- 239000004472 Lysine Substances 0.000 claims description 5
- KDXKERNSBIXSRK-UHFFFAOYSA-N Lysine Natural products NCCCCC(N)C(O)=O KDXKERNSBIXSRK-UHFFFAOYSA-N 0.000 claims description 5
- 239000004115 Sodium Silicate Substances 0.000 claims description 5
- 235000004279 alanine Nutrition 0.000 claims description 5
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 5
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims description 5
- 239000004327 boric acid Substances 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- 238000010790 dilution Methods 0.000 claims description 5
- 239000012895 dilution Substances 0.000 claims description 5
- 239000012153 distilled water Substances 0.000 claims description 5
- 239000011790 ferrous sulphate Substances 0.000 claims description 5
- 235000003891 ferrous sulphate Nutrition 0.000 claims description 5
- 239000012530 fluid Substances 0.000 claims description 5
- 235000013922 glutamic acid Nutrition 0.000 claims description 5
- 239000004220 glutamic acid Substances 0.000 claims description 5
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 claims description 5
- 229910000359 iron(II) sulfate Inorganic materials 0.000 claims description 5
- COLNVLDHVKWLRT-UHFFFAOYSA-N phenylalanine Natural products OC(=O)C(N)CC1=CC=CC=C1 COLNVLDHVKWLRT-UHFFFAOYSA-N 0.000 claims description 5
- 239000012429 reaction media Substances 0.000 claims description 5
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 5
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 5
- KZSNJWFQEVHDMF-BYPYZUCNSA-N L-valine Chemical compound CC(C)[C@H](N)C(O)=O KZSNJWFQEVHDMF-BYPYZUCNSA-N 0.000 claims description 4
- KZSNJWFQEVHDMF-UHFFFAOYSA-N Valine Natural products CC(C)C(N)C(O)=O KZSNJWFQEVHDMF-UHFFFAOYSA-N 0.000 claims description 4
- 125000004122 cyclic group Chemical group 0.000 claims description 4
- 239000004474 valine Substances 0.000 claims description 4
- 239000013522 chelant Substances 0.000 claims description 3
- 238000005303 weighing Methods 0.000 claims 4
- 239000007788 liquid Substances 0.000 claims 2
- 238000007865 diluting Methods 0.000 claims 1
- 238000004064 recycling Methods 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 150000001413 amino acids Chemical class 0.000 abstract description 7
- 230000009286 beneficial effect Effects 0.000 abstract description 5
- 235000015097 nutrients Nutrition 0.000 abstract description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 4
- 230000008635 plant growth Effects 0.000 abstract description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract description 3
- 239000011574 phosphorus Substances 0.000 abstract description 3
- 229910052698 phosphorus Inorganic materials 0.000 abstract description 3
- 239000002689 soil Substances 0.000 abstract description 3
- 239000011593 sulfur Substances 0.000 abstract description 3
- 229910052717 sulfur Inorganic materials 0.000 abstract description 3
- 102000004190 Enzymes Human genes 0.000 abstract description 2
- 108090000790 Enzymes Proteins 0.000 abstract description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 abstract description 2
- 230000008485 antagonism Effects 0.000 abstract description 2
- 230000003851 biochemical process Effects 0.000 abstract description 2
- 159000000007 calcium salts Chemical class 0.000 abstract description 2
- 210000000170 cell membrane Anatomy 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 230000012010 growth Effects 0.000 abstract description 2
- 229910021645 metal ion Inorganic materials 0.000 abstract description 2
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 2
- 230000035790 physiological processes and functions Effects 0.000 abstract description 2
- 239000002244 precipitate Substances 0.000 abstract 1
- 238000000746 purification Methods 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 description 9
- 239000006210 lotion Substances 0.000 description 8
- 238000002360 preparation method Methods 0.000 description 8
- 239000012141 concentrate Substances 0.000 description 7
- 238000002425 crystallisation Methods 0.000 description 7
- 230000008025 crystallization Effects 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 238000005119 centrifugation Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000001577 simple distillation Methods 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- 241000227653 Lycopersicon Species 0.000 description 3
- 235000007688 Lycopersicon esculentum Nutrition 0.000 description 2
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- NQPDZGIKBAWPEJ-UHFFFAOYSA-N valeric acid Chemical compound CCCCC(O)=O NQPDZGIKBAWPEJ-UHFFFAOYSA-N 0.000 description 2
- NWONKYPBYAMBJT-UHFFFAOYSA-L zinc sulfate Chemical compound [Zn+2].[O-]S([O-])(=O)=O NWONKYPBYAMBJT-UHFFFAOYSA-L 0.000 description 2
- 229960001763 zinc sulfate Drugs 0.000 description 2
- 229910000368 zinc sulfate Inorganic materials 0.000 description 2
- 230000007812 deficiency Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000004720 fertilization Effects 0.000 description 1
- 235000012041 food component Nutrition 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 230000002262 irrigation Effects 0.000 description 1
- 238000003973 irrigation Methods 0.000 description 1
- 235000016709 nutrition Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 230000009469 supplementation Effects 0.000 description 1
- 229940005605 valeric acid Drugs 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05C—NITROGENOUS FERTILISERS
- C05C5/00—Fertilisers containing other nitrates
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05G—MIXTURES OF FERTILISERS COVERED INDIVIDUALLY BY DIFFERENT SUBCLASSES OF CLASS C05; MIXTURES OF ONE OR MORE FERTILISERS WITH MATERIALS NOT HAVING A SPECIFIC FERTILISING ACTIVITY, e.g. PESTICIDES, SOIL-CONDITIONERS, WETTING AGENTS; FERTILISERS CHARACTERISED BY THEIR FORM
- C05G3/00—Mixtures of one or more fertilisers with additives not having a specially fertilising activity
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Pest Control & Pesticides (AREA)
- Fertilizers (AREA)
Abstract
Description
技术领域technical field
本发明涉及农作物肥料技术领域,具体涉及一种含Gly水溶肥料生产的方法。The invention relates to the technical field of crop fertilizers, in particular to a method for producing Gly-containing water-soluble fertilizers.
背景技术Background technique
水溶肥料易被农作物吸收,吸收利用率相对较高,是一个速效肥料,可以让种植者较快地看到肥料的效果和表现,随时可以根据作物不同长势对肥料配方作出调整;而且水溶肥料可以应用于喷滴灌等设施农业,实现水肥一体化,达到省水省肥省工的效能。现有的水溶肥料大多是通过中量元素和微量元素混合制得,部分水溶肥料还有指定种类的氨基酸,但是现有水溶肥料中的金属离子大都是以金属盐的形式存在,在施肥的过程中容易与土壤中的磷、硫等元素形成沉淀,从而降低植物的吸收率,而且现有的水溶肥料中含有的氨基酸种类较少,无法使植物的营养成分得到全面保证,因此,如何研制一种营养成分较为全面且有利于植物吸收的水溶肥料,成为了本领域技术人员亟待解决的技术问题。Water-soluble fertilizers are easily absorbed by crops, and their absorption and utilization rate is relatively high. It is applied to facility agriculture such as drip irrigation, realizes the integration of water and fertilizer, and achieves the efficiency of saving water, fertilizer and labor. Most of the existing water-soluble fertilizers are made by mixing medium and trace elements. Some water-soluble fertilizers also have specified types of amino acids, but most of the metal ions in the existing water-soluble fertilizers exist in the form of metal salts. During the fertilization process It is easy to form precipitation with phosphorus, sulfur and other elements in the soil, thereby reducing the absorption rate of plants, and the existing water-soluble fertilizers contain fewer amino acids, which cannot fully guarantee the nutritional content of plants. Therefore, how to develop a fertilizer A kind of water-soluble fertilizer which has more comprehensive nutritional components and is beneficial to plant absorption has become a technical problem to be solved urgently by those skilled in the art.
发明内容Contents of the invention
解决的技术问题Technical issues resolved
针对现有技术的不足,本发明提供了一种含Gly水溶肥料生产的方法,使生产的水溶肥料在保证植物营养成分全面补充的同时,还能够提高营养成分的吸收利用率,从而提高水溶肥料的应用前景。Aiming at the deficiencies in the prior art, the present invention provides a method for producing water-soluble fertilizers containing Gly, so that the water-soluble fertilizers produced can also improve the absorption and utilization rate of nutrients while ensuring the comprehensive supplementation of plant nutrients, thereby improving the production efficiency of water-soluble fertilizers. application prospects.
技术方案Technical solutions
为实现以上目的,本发明通过以下技术方案予以实现:To achieve the above object, the present invention is achieved through the following technical solutions:
一种含Gly水溶肥料生产的方法,所述方法包括以下步骤:A kind of method that contains Gly water-soluble fertilizer production, described method comprises the following steps:
Step1、量取100重量份甘氨酸浓缩母液备用,接着使用等量的甲醇对甘氨酸浓缩母液进行稀释,稀释结束后过滤去掉杂质,将所得溶液加入至电渗析器的淡室料桶中,并向电渗析器的浓室料桶中加入蒸馏水,经电渗析分离后得到淡室溶液和浓室溶液,将淡室溶液在70-100℃的温度下加热浓缩,直至甘氨酸结晶析出,将结晶物通过过滤与母液分离,干燥后既得精品甘氨酸,结晶过滤后的母液可循环使用;Step1, measure 100 parts by weight of glycine concentrated mother liquor for later use, then use an equal amount of methanol to dilute the glycine concentrated mother liquor, filter to remove impurities after dilution, add the resulting solution to the dilute chamber material tank of the electrodialyzer, and send to the electrodialyzer Distilled water is added to the thick chamber barrel of the dialyzer, and the light chamber solution and the concentrated chamber solution are obtained after separation by electrodialysis. The light chamber solution is heated and concentrated at a temperature of 70-100°C until glycine crystallizes, and the crystals are filtered through Separated from the mother liquor, dried to obtain high-quality glycine, and the mother liquor after crystallization and filtration can be recycled;
Step2、按照2:3的摩尔比称取四水硝酸钙和Step1中的精品甘氨酸与去离子水进行混合,以300-400r/min的速度搅拌5-10min后制成混悬液,使用盐酸或氨水将混悬液pH调至5.5并将温度加热至50℃,然后将混悬液倒入高压流体纳米磨中进行处理,直至混悬液变清为止,对变清后的混悬液进行低温减压干燥,再用100-200目筛网过滤成细粉,所得记作甘氨酸螯合钙;Step2. Weigh calcium nitrate tetrahydrate and the high-quality glycine in Step1 and deionized water according to the molar ratio of 2:3, mix them with deionized water, stir at a speed of 300-400r/min for 5-10min to make a suspension, use hydrochloric acid or Ammonia water adjusts the pH of the suspension to 5.5 and heats the temperature to 50°C, then pours the suspension into a high-pressure fluid nanomill for processing until the suspension becomes clear, and then cools the clear suspension Dry under reduced pressure, then filter into fine powder with 100-200 mesh sieve, and the gained is recorded as glycine chelated calcium;
Step3、称取一定量的复合氨基酸溶解于重量为其2-3倍的去离子水中,过滤去除不溶物后使用氢氧化钠溶液调节pH至5,接着加入重量为复合氨基酸20-30%的七水硫酸锌,在60℃的水浴温度中反应30min,反应后加热浓缩并进行冷却结晶,对结晶物进行过滤和干燥,所得记作复合氨基酸螯合锌;Step3. Weigh a certain amount of compound amino acid and dissolve it in deionized water 2-3 times its weight. After removing the insoluble matter by filtration, use sodium hydroxide solution to adjust the pH to 5, and then add 20-30% of the weight of the compound amino acid. Zinc sulfate water, reacted in a water bath temperature of 60°C for 30 minutes, heated and concentrated after the reaction, cooled and crystallized, filtered and dried the crystals, and the obtained was recorded as compound amino acid chelated zinc;
Step4、按照重量份计称取58-60份取甘氨酸浓缩母液、8-9份六水硝酸镁、5-8份中量元素、3-5份微量元素、15-18份Step2中的甘氨酸螯合钙、4-5份Step3中的复合氨基酸螯合锌和85-90份去离子水备用;Step4, take 58-60 parts by weight to get concentrated glycine mother liquor, 8-9 parts of magnesium nitrate hexahydrate, 5-8 parts of medium elements, 3-5 parts of trace elements, 15-18 parts of glycine chelate in Step2 Calcium complex, 4-5 parts of compound amino acid chelated zinc in Step3 and 85-90 parts of deionized water are standby;
Step5、将Step4中的甘氨酸浓缩母液与去离子水中的一半进行混合,搅拌均匀后加入上述重量份的甘氨酸螯合钙和复合氨基酸螯合锌,并进行再次搅拌,所得记作第一组分;Step5. Mix the glycine concentrated mother liquor in Step4 with half of the deionized water, stir evenly, add the above-mentioned glycine chelated calcium and compound amino acid chelated zinc, and stir again, and the obtained is recorded as the first component;
Step6、将Step4中的六水硝酸镁、中量元素、微量元素和余量的去离子水进行混合,搅拌均匀后所得记作第二组分;Step6, the magnesium nitrate hexahydrate in Step4, middle element, trace element and the deionized water of surplus are mixed, after stirring, the gained is recorded as the second component;
Step7、将第一组分和第二组分进行混合,搅拌均匀后过滤去除杂质,接着加热浓缩至原体积的一半,所得即为含Gly水溶肥料。Step7. Mix the first component and the second component, stir evenly, filter to remove impurities, then heat and concentrate to half of the original volume, and the obtained water-soluble fertilizer containing Gly.
更进一步地,所述甘氨酸浓缩母液的制备方法包括以下步骤:Further, the preparation method of the concentrated glycine mother liquor comprises the following steps:
步骤1、向反应器中倒入氯乙酸、甲醇和乌洛托品,搅拌溶解后缓慢通入液氨,在58-60℃的温度条件下进行合成反应2h,在反应的过程中维持反应体系的pH为7-8,其中,氯乙酸、甲醇和乌洛托品的摩尔比为1:7.5:0.2;Step 1. Pour chloroacetic acid, methanol and urotropine into the reactor, stir and dissolve, then slowly feed liquid ammonia, carry out the synthesis reaction at a temperature of 58-60°C for 2 hours, and maintain the reaction system during the reaction The pH is 7-8, wherein the molar ratio of chloroacetic acid, methanol and urotropine is 1:7.5:0.2;
步骤2、步骤1的反应结束后继续保温直至有晶体析出,接着冷却至室温并离心过滤,离心后得到母液和结晶物,使用少量甲醇对结晶物洗涤2次,将洗涤所得的洗液与上述母液进行混合,所得记作循环反应溶剂;Step 2, after the reaction of step 1, continue to keep warm until crystals are precipitated, then cool to room temperature and centrifugally filter, obtain mother liquor and crystals after centrifugation, use a small amount of methanol to wash the crystals twice, and wash the obtained lotion with the above-mentioned The mother liquor is mixed, and the gained is recorded as the circulating reaction solvent;
步骤3、将步骤2中的循环反应溶剂作为反应介质供下次循环反应使用,直到最后一次循环反应结束后得到母液和结晶物;Step 3, using the circulating reaction solvent in step 2 as the reaction medium for the next circulating reaction, until the last circulating reaction ends to obtain mother liquor and crystals;
步骤4、使用甲醇对步骤3中的结晶物进行洗涤2次,洗涤后的洗液与步骤3中的母液进行混合,混合后进行简单蒸馏,所得即为甘氨酸浓缩母液。Step 4, washing the crystals in step 3 twice with methanol, mixing the washed lotion with the mother liquor in step 3, and performing simple distillation after mixing to obtain concentrated glycine mother liquor.
更进一步地,所述步骤1中的搅拌速度为500-600r/min,所述步骤2中的离心转速为7000-8000r/min。Furthermore, the stirring speed in the step 1 is 500-600r/min, and the centrifugal speed in the step 2 is 7000-8000r/min.
更进一步地,所述步骤3中循环反应的次数为3-4次。Furthermore, the number of cyclic reactions in the step 3 is 3-4 times.
更进一步地,所述Step1的加热浓缩需要不断搅拌的情况下进行。Furthermore, the heating and concentration of Step 1 needs to be carried out under the condition of constant stirring.
更进一步地,所述Step2中去离子水的量为四水硝酸钙和精品甘氨酸总量的3-4倍。Further, the amount of deionized water in the Step2 is 3-4 times of the total amount of calcium nitrate tetrahydrate and refined glycine.
更进一步地,所述Step3中复合氨基酸的制备方法为:按照重量份计称取17-18份赖氨酸、1-2份谷氨酸、0.3-0.5份丙氨酸、0.03-0.05份缬氨酸和0.1-0.3份苯丙氨酸进行混合,混合均匀后即为复合氨基酸。Further, the preparation method of the compound amino acid in the Step3 is: weigh 17-18 parts of lysine, 1-2 parts of glutamic acid, 0.3-0.5 parts of alanine, 0.03-0.05 parts of valeric acid in parts by weight Amino acid and 0.1-0.3 parts of phenylalanine are mixed, and the compound amino acid is obtained after mixing evenly.
更进一步地,所述Step4中的中量元素为水合硅酸钠。Furthermore, the middle element in the Step4 is hydrated sodium silicate.
更进一步地,所述Step4中的微量元素为硼酸和硫酸亚铁按同等重量比混合制得。Furthermore, the trace elements in Step4 are obtained by mixing boric acid and ferrous sulfate in equal weight ratios.
更进一步地,所述Step5和Step6中的搅拌速度为600-800r/min。Further, the stirring speed in Step5 and Step6 is 600-800r/min.
有益效果Beneficial effect
本发明提供了一种含Gly水溶肥料生产的方法,与现有公知技术相比,本发明的具有如下有益效果:The invention provides a method for producing Gly-containing water-soluble fertilizers. Compared with the prior known technology, the invention has the following beneficial effects:
本发明通过电渗析法对甘氨酸浓缩母液进行提纯,并使提纯制得的精品甘氨酸与四水硝酸钙进行反应制得甘氨酸螯合钙,能够防止钙盐与磷、硫等营养元素形成沉淀的情况发生,通过甘氨酸螯合钙的作用能够增强植物细胞膜的稳定性,还能够参与植物生理生化过程及酶活性的调控,有利于植物的生长;其次,以多种氨基酸混合制得的复合氨基酸和七水硫酸锌制成复合氨基酸螯合锌,能够向植物提供微量元素及多种氨基酸成分,在通过复合氨基酸为植物生长提供氮源的同时,还能够通过微量元素锌来抵抗土壤的干扰、缓解金属离子拮抗,为植物提供稳定的生长环境;最后,通过六水硝酸镁、中量元素以及微量元素的加入,能够为植物提供更充足的养分,从而使本发明生产的含Gly水溶肥料具有更好的应用前景。The present invention purifies the concentrated glycine mother liquor by electrodialysis, and reacts the purified refined glycine with calcium nitrate tetrahydrate to prepare glycine chelated calcium, which can prevent calcium salt from forming precipitation with phosphorus, sulfur and other nutrient elements Glycine chelated calcium can enhance the stability of plant cell membranes, and can also participate in the regulation of plant physiological and biochemical processes and enzyme activities, which is beneficial to the growth of plants; secondly, compound amino acids and seven Zinc sulfate water is made of compound amino acid chelated zinc, which can provide plants with trace elements and a variety of amino acid components. While providing nitrogen sources for plant growth through compound amino acids, it can also resist soil interference and relieve metal stress through the trace element zinc. Ion antagonism provides a stable growth environment for plants; finally, through the addition of magnesium nitrate hexahydrate, medium elements and trace elements, more sufficient nutrients can be provided for plants, so that the Gly-containing water-soluble fertilizer produced by the present invention has better application prospects.
具体实施方式detailed description
为使本发明实施例的目的、技术方案和优点更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有作出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。In order to make the purpose, technical solutions and advantages of the embodiments of the present invention clearer, the technical solutions in the embodiments of the present invention will be clearly and completely described below. Obviously, the described embodiments are part of the embodiments of the present invention, not all of them. the embodiment. Based on the embodiments of the present invention, all other embodiments obtained by persons of ordinary skill in the art without creative efforts fall within the protection scope of the present invention.
实施例1:Example 1:
本实施例的一种含Gly水溶肥料生产的方法,方法包括以下步骤:A kind of method that contains Gly water-soluble fertilizer production of the present embodiment, the method comprises the following steps:
Step1、量取100重量份甘氨酸浓缩母液备用,接着使用等量的甲醇对甘氨酸浓缩母液进行稀释,稀释结束后过滤去掉杂质,将所得溶液加入至电渗析器的淡室料桶中,并向电渗析器的浓室料桶中加入蒸馏水,经电渗析分离后得到淡室溶液和浓室溶液,将淡室溶液在70℃的温度下加热浓缩,直至甘氨酸结晶析出,将结晶物通过过滤与母液分离,干燥后既得精品甘氨酸,结晶过滤后的母液可循环使用;Step1, measure 100 parts by weight of glycine concentrated mother liquor for later use, then use an equal amount of methanol to dilute the glycine concentrated mother liquor, filter to remove impurities after dilution, add the resulting solution to the dilute chamber material tank of the electrodialyzer, and send to the electrodialyzer Distilled water is added to the thick chamber barrel of the dialyzer, and the light chamber solution and the concentrated chamber solution are obtained after separation by electrodialysis. The light chamber solution is heated and concentrated at a temperature of 70°C until glycine crystals are precipitated, and the crystals are filtered and mixed with the mother liquor. After separation and drying, high-quality glycine is obtained, and the mother liquor after crystallization and filtration can be recycled;
Step2、按照2:3的摩尔比称取四水硝酸钙和Step1中的精品甘氨酸与去离子水进行混合,以300r/min的速度搅拌5min后制成混悬液,使用盐酸或氨水将混悬液pH调至5.5并将温度加热至50℃,然后将混悬液倒入高压流体纳米磨中进行处理,直至混悬液变清为止,对变清后的混悬液进行低温减压干燥,再用100目筛网过滤成细粉,所得记作甘氨酸螯合钙;Step2. Weigh calcium nitrate tetrahydrate and the high-quality glycine in Step1 and deionized water according to the molar ratio of 2:3, mix them with deionized water, stir at a speed of 300r/min for 5min to make a suspension, and use hydrochloric acid or ammonia water to dissolve the suspension The pH of the solution is adjusted to 5.5 and the temperature is heated to 50°C, then the suspension is poured into a high-pressure fluid nanomill for processing until the suspension becomes clear, and the clear suspension is dried under reduced pressure at low temperature, Filter it into a fine powder with a 100-mesh sieve, and the gained is recorded as glycine chelated calcium;
Step3、称取一定量的复合氨基酸溶解于重量为其2倍的去离子水中,过滤去除不溶物后使用氢氧化钠溶液调节pH至5,接着加入重量为复合氨基酸20%的七水硫酸锌,在60℃的水浴温度中反应30min,反应后加热浓缩并进行冷却结晶,对结晶物进行过滤和干燥,所得记作复合氨基酸螯合锌;Step3, take a certain amount of compound amino acid and dissolve it in deionized water twice its weight, filter and remove insoluble matter, use sodium hydroxide solution to adjust the pH to 5, then add zinc sulfate heptahydrate whose weight is 20% of compound amino acid, React in a water bath temperature of 60°C for 30 minutes, heat and concentrate after the reaction, and carry out cooling and crystallization, filter and dry the crystals, and the obtained is recorded as the compound amino acid chelated zinc;
Step4、按照重量份计称取58份取甘氨酸浓缩母液、8份六水硝酸镁、5份中量元素、3份微量元素、15份Step2中的甘氨酸螯合钙、4份Step3中的复合氨基酸螯合锌和85份去离子水备用;Step4, take 58 parts by weight to take concentrated glycine mother liquor, 8 parts of magnesium nitrate hexahydrate, 5 parts of medium elements, 3 parts of trace elements, 15 parts of glycine chelated calcium in Step2, 4 parts of compound amino acids in Step3 Chelated zinc and 85 parts of deionized water are standby;
Step5、将Step4中的甘氨酸浓缩母液与去离子水中的一半进行混合,搅拌均匀后加入上述重量份的甘氨酸螯合钙和复合氨基酸螯合锌,并进行再次搅拌,所得记作第一组分;Step5. Mix the glycine concentrated mother liquor in Step4 with half of the deionized water, stir evenly, add the above-mentioned glycine chelated calcium and compound amino acid chelated zinc, and stir again, and the obtained is recorded as the first component;
Step6、将Step4中的六水硝酸镁、中量元素、微量元素和余量的去离子水进行混合,搅拌均匀后所得记作第二组分;Step6, the magnesium nitrate hexahydrate in Step4, middle element, trace element and the deionized water of surplus are mixed, after stirring, the gained is recorded as the second component;
Step7、将第一组分和第二组分进行混合,搅拌均匀后过滤去除杂质,接着加热浓缩至原体积的一半,所得即为含Gly水溶肥料。Step7. Mix the first component and the second component, stir evenly, filter to remove impurities, then heat and concentrate to half of the original volume, and the obtained water-soluble fertilizer containing Gly.
甘氨酸浓缩母液的制备方法包括以下步骤:The preparation method of glycine concentrated mother liquor comprises the following steps:
步骤1、向反应器中倒入氯乙酸、甲醇和乌洛托品,搅拌溶解后缓慢通入液氨,在58℃的温度条件下进行合成反应2h,在反应的过程中维持反应体系的pH为7,其中,氯乙酸、甲醇和乌洛托品的摩尔比为1:7.5:0.2;Step 1. Pour chloroacetic acid, methanol and urotropine into the reactor, stir and dissolve, then slowly feed liquid ammonia, carry out the synthesis reaction at a temperature of 58°C for 2 hours, and maintain the pH of the reaction system during the reaction is 7, wherein the molar ratio of chloroacetic acid, methanol and urotropine is 1:7.5:0.2;
步骤2、步骤1的反应结束后继续保温直至有晶体析出,接着冷却至室温并离心过滤,离心后得到母液和结晶物,使用少量甲醇对结晶物洗涤2次,将洗涤所得的洗液与上述母液进行混合,所得记作循环反应溶剂;Step 2, after the reaction of step 1, continue to keep warm until crystals are precipitated, then cool to room temperature and centrifugally filter, obtain mother liquor and crystals after centrifugation, use a small amount of methanol to wash the crystals twice, and wash the obtained lotion with the above-mentioned The mother liquor is mixed, and the gained is recorded as the circulating reaction solvent;
步骤3、将步骤2中的循环反应溶剂作为反应介质供下次循环反应使用,直到最后一次循环反应结束后得到母液和结晶物;Step 3, using the circulating reaction solvent in step 2 as the reaction medium for the next circulating reaction, until the last circulating reaction ends to obtain mother liquor and crystals;
步骤4、使用甲醇对步骤3中的结晶物进行洗涤2次,洗涤后的洗液与步骤3中的母液进行混合,混合后进行简单蒸馏,所得即为甘氨酸浓缩母液。Step 4, washing the crystals in step 3 twice with methanol, mixing the washed lotion with the mother liquor in step 3, and performing simple distillation after mixing to obtain concentrated glycine mother liquor.
步骤1中的搅拌速度为500r/min,步骤2中的离心转速为7000r/min。The stirring speed in step 1 is 500r/min, and the centrifugal speed in step 2 is 7000r/min.
步骤3中循环反应的次数为3次。The number of cycle reactions in step 3 is 3 times.
Step1的加热浓缩需要不断搅拌的情况下进行。The heating concentration of Step1 needs to be carried out under the condition of constant stirring.
Step2中去离子水的量为四水硝酸钙和精品甘氨酸总量的3倍。The amount of deionized water in Step2 is 3 times of the total amount of calcium nitrate tetrahydrate and high-quality glycine.
Step3中复合氨基酸的制备方法为:按照重量份计称取17份赖氨酸、1份谷氨酸、0.3份丙氨酸、0.03份缬氨酸和0.1份苯丙氨酸进行混合,混合均匀后即为复合氨基酸。The preparation method of the compound amino acid in Step3 is: weigh 17 parts of lysine, 1 part of glutamic acid, 0.3 part of alanine, 0.03 part of valine and 0.1 part of phenylalanine in parts by weight and mix them evenly After that is the compound amino acid.
Step4中的中量元素为水合硅酸钠。The middle element in Step4 is hydrated sodium silicate.
Step4中的微量元素为硼酸和硫酸亚铁按同等重量比混合制得。Trace elements in Step4 are obtained by mixing boric acid and ferrous sulfate in equal weight ratios.
Step5和Step6中的搅拌速度为600r/min。The stirring speed in Step5 and Step6 is 600r/min.
实施例2:Example 2:
本实施例的一种含Gly水溶肥料生产的方法,方法包括以下步骤:A kind of method that contains Gly water-soluble fertilizer production of the present embodiment, the method comprises the following steps:
Step1、量取100重量份甘氨酸浓缩母液备用,接着使用等量的甲醇对甘氨酸浓缩母液进行稀释,稀释结束后过滤去掉杂质,将所得溶液加入至电渗析器的淡室料桶中,并向电渗析器的浓室料桶中加入蒸馏水,经电渗析分离后得到淡室溶液和浓室溶液,将淡室溶液在100℃的温度下加热浓缩,直至甘氨酸结晶析出,将结晶物通过过滤与母液分离,干燥后既得精品甘氨酸,结晶过滤后的母液可循环使用;Step1, measure 100 parts by weight of glycine concentrated mother liquor for later use, then use an equal amount of methanol to dilute the glycine concentrated mother liquor, filter to remove impurities after dilution, add the resulting solution to the dilute chamber material tank of the electrodialyzer, and send to the electrodialyzer Distilled water is added to the thick chamber barrel of the dialyzer, and the light chamber solution and the concentrated chamber solution are obtained after separation by electrodialysis. The light chamber solution is heated and concentrated at a temperature of 100°C until glycine crystallizes, and the crystals are filtered and mixed with the mother liquor. After separation and drying, high-quality glycine is obtained, and the mother liquor after crystallization and filtration can be recycled;
Step2、按照2:3的摩尔比称取四水硝酸钙和Step1中的精品甘氨酸与去离子水进行混合,以400r/min的速度搅拌10min后制成混悬液,使用盐酸或氨水将混悬液pH调至5.5并将温度加热至50℃,然后将混悬液倒入高压流体纳米磨中进行处理,直至混悬液变清为止,对变清后的混悬液进行低温减压干燥,再用200目筛网过滤成细粉,所得记作甘氨酸螯合钙;Step2. Weigh calcium nitrate tetrahydrate and the high-quality glycine in Step1 and deionized water according to the molar ratio of 2:3, mix them with deionized water, stir at a speed of 400r/min for 10min to make a suspension, and use hydrochloric acid or ammonia water to dissolve the suspension The pH of the solution is adjusted to 5.5 and the temperature is heated to 50°C, then the suspension is poured into a high-pressure fluid nanomill for processing until the suspension becomes clear, and the clear suspension is dried under reduced pressure at low temperature, Filter it into a fine powder with a 200-mesh sieve, and the gained is recorded as glycine chelated calcium;
Step3、称取一定量的复合氨基酸溶解于重量为其3倍的去离子水中,过滤去除不溶物后使用氢氧化钠溶液调节pH至5,接着加入重量为复合氨基酸30%的七水硫酸锌,在60℃的水浴温度中反应30min,反应后加热浓缩并进行冷却结晶,对结晶物进行过滤和干燥,所得记作复合氨基酸螯合锌;Step3, take a certain amount of compound amino acid and dissolve it in deionized water whose weight is 3 times, filter and remove insoluble matter, use sodium hydroxide solution to adjust the pH to 5, then add zinc sulfate heptahydrate whose weight is 30% of compound amino acid, React in a water bath temperature of 60°C for 30 minutes, heat and concentrate after the reaction, and carry out cooling and crystallization, filter and dry the crystals, and the obtained is recorded as the compound amino acid chelated zinc;
Step4、按照重量份计称取60份取甘氨酸浓缩母液、9份六水硝酸镁、8份中量元素、5份微量元素、18份Step2中的甘氨酸螯合钙、5份Step3中的复合氨基酸螯合锌和90份去离子水备用;Step4, take by weight 60 parts of concentrated glycine mother liquor, 9 parts of magnesium nitrate hexahydrate, 8 parts of medium elements, 5 parts of trace elements, 18 parts of glycine chelated calcium in Step2, 5 parts of compound amino acids in Step3 Chelated zinc and 90 parts of deionized water are standby;
Step5、将Step4中的甘氨酸浓缩母液与去离子水中的一半进行混合,搅拌均匀后加入上述重量份的甘氨酸螯合钙和复合氨基酸螯合锌,并进行再次搅拌,所得记作第一组分;Step5. Mix the glycine concentrated mother liquor in Step4 with half of the deionized water, stir evenly, add the above-mentioned glycine chelated calcium and compound amino acid chelated zinc, and stir again, and the obtained is recorded as the first component;
Step6、将Step4中的六水硝酸镁、中量元素、微量元素和余量的去离子水进行混合,搅拌均匀后所得记作第二组分;Step6, the magnesium nitrate hexahydrate in Step4, middle element, trace element and the deionized water of surplus are mixed, after stirring, the gained is recorded as the second component;
Step7、将第一组分和第二组分进行混合,搅拌均匀后过滤去除杂质,接着加热浓缩至原体积的一半,所得即为含Gly水溶肥料。Step7. Mix the first component and the second component, stir evenly, filter to remove impurities, then heat and concentrate to half of the original volume, and the obtained water-soluble fertilizer containing Gly.
甘氨酸浓缩母液的制备方法包括以下步骤:The preparation method of glycine concentrated mother liquor comprises the following steps:
步骤1、向反应器中倒入氯乙酸、甲醇和乌洛托品,搅拌溶解后缓慢通入液氨,在60℃的温度条件下进行合成反应2h,在反应的过程中维持反应体系的pH为8,其中,氯乙酸、甲醇和乌洛托品的摩尔比为1:7.5:0.2;Step 1. Pour chloroacetic acid, methanol and urotropine into the reactor, stir and dissolve, then slowly feed liquid ammonia, carry out the synthesis reaction at 60°C for 2 hours, and maintain the pH of the reaction system during the reaction is 8, wherein the molar ratio of chloroacetic acid, methanol and urotropine is 1:7.5:0.2;
步骤2、步骤1的反应结束后继续保温直至有晶体析出,接着冷却至室温并离心过滤,离心后得到母液和结晶物,使用少量甲醇对结晶物洗涤2次,将洗涤所得的洗液与上述母液进行混合,所得记作循环反应溶剂;Step 2, after the reaction of step 1, continue to keep warm until crystals are precipitated, then cool to room temperature and centrifugally filter, obtain mother liquor and crystals after centrifugation, use a small amount of methanol to wash the crystals twice, and wash the obtained lotion with the above-mentioned The mother liquor is mixed, and the gained is recorded as the circulating reaction solvent;
步骤3、将步骤2中的循环反应溶剂作为反应介质供下次循环反应使用,直到最后一次循环反应结束后得到母液和结晶物;Step 3, using the circulating reaction solvent in step 2 as the reaction medium for the next circulating reaction, until the last circulating reaction ends to obtain mother liquor and crystals;
步骤4、使用甲醇对步骤3中的结晶物进行洗涤2次,洗涤后的洗液与步骤3中的母液进行混合,混合后进行简单蒸馏,所得即为甘氨酸浓缩母液。Step 4, washing the crystals in step 3 twice with methanol, mixing the washed lotion with the mother liquor in step 3, and performing simple distillation after mixing to obtain concentrated glycine mother liquor.
步骤1中的搅拌速度为600r/min,步骤2中的离心转速为8000r/min。The stirring speed in step 1 is 600r/min, and the centrifugal speed in step 2 is 8000r/min.
步骤3中循环反应的次数为4次。The number of cycle reactions in step 3 is 4 times.
Step1的加热浓缩需要不断搅拌的情况下进行。The heating concentration of Step1 needs to be carried out under the condition of constant stirring.
Step2中去离子水的量为四水硝酸钙和精品甘氨酸总量的4倍。The amount of deionized water in Step2 is 4 times of the total amount of calcium nitrate tetrahydrate and high-quality glycine.
Step3中复合氨基酸的制备方法为:按照重量份计称取18份赖氨酸、2份谷氨酸、0.5份丙氨酸、0.05份缬氨酸和0.3份苯丙氨酸进行混合,混合均匀后即为复合氨基酸。The preparation method of the compound amino acid in Step3 is: weigh 18 parts of lysine, 2 parts of glutamic acid, 0.5 part of alanine, 0.05 part of valine and 0.3 part of phenylalanine in parts by weight and mix them evenly After that is the compound amino acid.
Step4中的中量元素为水合硅酸钠。The middle element in Step4 is hydrated sodium silicate.
Step4中的微量元素为硼酸和硫酸亚铁按同等重量比混合制得。Trace elements in Step4 are obtained by mixing boric acid and ferrous sulfate in equal weight ratios.
Step5和Step6中的搅拌速度为600r/min。The stirring speed in Step5 and Step6 is 600r/min.
实施例3:Example 3:
本实施例的一种含Gly水溶肥料生产的方法,方法包括以下步骤:A kind of method that contains Gly water-soluble fertilizer production of the present embodiment, the method comprises the following steps:
Step1、量取100重量份甘氨酸浓缩母液备用,接着使用等量的甲醇对甘氨酸浓缩母液进行稀释,稀释结束后过滤去掉杂质,将所得溶液加入至电渗析器的淡室料桶中,并向电渗析器的浓室料桶中加入蒸馏水,经电渗析分离后得到淡室溶液和浓室溶液,将淡室溶液在80℃的温度下加热浓缩,直至甘氨酸结晶析出,将结晶物通过过滤与母液分离,干燥后既得精品甘氨酸,结晶过滤后的母液可循环使用;Step1, measure 100 parts by weight of glycine concentrated mother liquor for later use, then use an equal amount of methanol to dilute the glycine concentrated mother liquor, filter to remove impurities after dilution, add the resulting solution to the dilute chamber material tank of the electrodialyzer, and send to the electrodialyzer Distilled water is added to the thick chamber barrel of the dialyzer, and the light chamber solution and the concentrated chamber solution are obtained after separation by electrodialysis. The light chamber solution is heated and concentrated at a temperature of 80°C until glycine crystals are precipitated, and the crystals are filtered and mixed with the mother liquor. After separation and drying, high-quality glycine is obtained, and the mother liquor after crystallization and filtration can be recycled;
Step2、按照2:3的摩尔比称取四水硝酸钙和Step1中的精品甘氨酸与去离子水进行混合,以400r/min的速度搅拌8min后制成混悬液,使用盐酸或氨水将混悬液pH调至5.5并将温度加热至50℃,然后将混悬液倒入高压流体纳米磨中进行处理,直至混悬液变清为止,对变清后的混悬液进行低温减压干燥,再用200目筛网过滤成细粉,所得记作甘氨酸螯合钙;Step2. Weigh calcium nitrate tetrahydrate and the high-quality glycine in Step1 and deionized water according to the molar ratio of 2:3 and mix them with deionized water. Stir at a speed of 400r/min for 8 minutes to make a suspension. Use hydrochloric acid or ammonia water to dissolve the suspension The pH of the solution is adjusted to 5.5 and the temperature is heated to 50°C, then the suspension is poured into a high-pressure fluid nanomill for processing until the suspension becomes clear, and the clear suspension is dried under reduced pressure at low temperature, Filter it into a fine powder with a 200-mesh sieve, and the gained is recorded as glycine chelated calcium;
Step3、称取一定量的复合氨基酸溶解于重量为其3倍的去离子水中,过滤去除不溶物后使用氢氧化钠溶液调节pH至5,接着加入重量为复合氨基酸25%的七水硫酸锌,在60℃的水浴温度中反应30min,反应后加热浓缩并进行冷却结晶,对结晶物进行过滤和干燥,所得记作复合氨基酸螯合锌;Step3, take a certain amount of compound amino acid and dissolve it in deionized water whose weight is 3 times, filter and remove insoluble matter, use sodium hydroxide solution to adjust the pH to 5, then add zinc sulfate heptahydrate whose weight is 25% of compound amino acid, React in a water bath temperature of 60°C for 30 minutes, heat and concentrate after the reaction, and carry out cooling and crystallization, filter and dry the crystals, and the obtained is recorded as the compound amino acid chelated zinc;
Step4、按照重量份计称取59份取甘氨酸浓缩母液、9份六水硝酸镁、7份中量元素、4份微量元素、16份Step2中的甘氨酸螯合钙、5份Step3中的复合氨基酸螯合锌和88份去离子水备用;Step4, take by weight 59 parts of glycine concentrated mother liquor, 9 parts of magnesium nitrate hexahydrate, 7 parts of medium elements, 4 parts of trace elements, 16 parts of glycine chelated calcium in Step2, 5 parts of compound amino acids in Step3 Chelated zinc and 88 parts of deionized water are standby;
Step5、将Step4中的甘氨酸浓缩母液与去离子水中的一半进行混合,搅拌均匀后加入上述重量份的甘氨酸螯合钙和复合氨基酸螯合锌,并进行再次搅拌,所得记作第一组分;Step5. Mix the glycine concentrated mother liquor in Step4 with half of the deionized water, stir evenly, add the above-mentioned glycine chelated calcium and compound amino acid chelated zinc, and stir again, and the obtained is recorded as the first component;
Step6、将Step4中的六水硝酸镁、中量元素、微量元素和余量的去离子水进行混合,搅拌均匀后所得记作第二组分;Step6, the magnesium nitrate hexahydrate in Step4, middle element, trace element and the deionized water of surplus are mixed, after stirring, the gained is recorded as the second component;
Step7、将第一组分和第二组分进行混合,搅拌均匀后过滤去除杂质,接着加热浓缩至原体积的一半,所得即为含Gly水溶肥料。Step7. Mix the first component and the second component, stir evenly, filter to remove impurities, then heat and concentrate to half of the original volume, and the obtained water-soluble fertilizer containing Gly.
甘氨酸浓缩母液的制备方法包括以下步骤:The preparation method of glycine concentrated mother liquor comprises the following steps:
步骤1、向反应器中倒入氯乙酸、甲醇和乌洛托品,搅拌溶解后缓慢通入液氨,在59℃的温度条件下进行合成反应2h,在反应的过程中维持反应体系的pH为8,其中,氯乙酸、甲醇和乌洛托品的摩尔比为1:7.5:0.2;Step 1. Pour chloroacetic acid, methanol and urotropine into the reactor, stir and dissolve, then slowly feed liquid ammonia, carry out the synthesis reaction at 59°C for 2 hours, and maintain the pH of the reaction system during the reaction is 8, wherein the molar ratio of chloroacetic acid, methanol and urotropine is 1:7.5:0.2;
步骤2、步骤1的反应结束后继续保温直至有晶体析出,接着冷却至室温并离心过滤,离心后得到母液和结晶物,使用少量甲醇对结晶物洗涤2次,将洗涤所得的洗液与上述母液进行混合,所得记作循环反应溶剂;Step 2, after the reaction of step 1, continue to keep warm until crystals are precipitated, then cool to room temperature and centrifugally filter, obtain mother liquor and crystals after centrifugation, use a small amount of methanol to wash the crystals twice, and wash the obtained lotion with the above-mentioned The mother liquor is mixed, and the gained is recorded as the circulating reaction solvent;
步骤3、将步骤2中的循环反应溶剂作为反应介质供下次循环反应使用,直到最后一次循环反应结束后得到母液和结晶物;Step 3, using the circulating reaction solvent in step 2 as the reaction medium for the next circulating reaction, until the last circulating reaction ends to obtain mother liquor and crystals;
步骤4、使用甲醇对步骤3中的结晶物进行洗涤2次,洗涤后的洗液与步骤3中的母液进行混合,混合后进行简单蒸馏,所得即为甘氨酸浓缩母液。Step 4, washing the crystals in step 3 twice with methanol, mixing the washed lotion with the mother liquor in step 3, and performing simple distillation after mixing to obtain concentrated glycine mother liquor.
步骤1中的搅拌速度为500r/min,步骤2中的离心转速为8000r/min。The stirring speed in step 1 is 500r/min, and the centrifugal speed in step 2 is 8000r/min.
步骤3中循环反应的次数为3次。The number of cycle reactions in step 3 is 3 times.
Step1的加热浓缩需要不断搅拌的情况下进行。The heating concentration of Step1 needs to be carried out under the condition of constant stirring.
Step2中去离子水的量为四水硝酸钙和精品甘氨酸总量的3倍。The amount of deionized water in Step2 is 3 times of the total amount of calcium nitrate tetrahydrate and high-quality glycine.
Step3中复合氨基酸的制备方法为:按照重量份计称取18份赖氨酸、1份谷氨酸、0.4份丙氨酸、0.04份缬氨酸和0.2份苯丙氨酸进行混合,混合均匀后即为复合氨基酸。The preparation method of the compound amino acid in Step3 is: weigh 18 parts of lysine, 1 part of glutamic acid, 0.4 part of alanine, 0.04 part of valine and 0.2 part of phenylalanine in parts by weight and mix them evenly After that is the compound amino acid.
Step4中的中量元素为水合硅酸钠。The middle element in Step4 is hydrated sodium silicate.
Step4中的微量元素为硼酸和硫酸亚铁按同等重量比混合制得。Trace elements in Step4 are obtained by mixing boric acid and ferrous sulfate in equal weight ratios.
Step5和Step6中的搅拌速度为700r/min。The stirring speed in Step5 and Step6 is 700r/min.
对比例:Comparative example:
于市面上随机抽取的一种含氨基酸水溶肥料。A water-soluble fertilizer containing amino acids randomly selected from the market.
性能检测performance testing
在实验田中随机划分4块3米×10米的试验田,并按照同样的种植方式种植同一品种的番茄,留取一块试验田不喷施肥料记作为空白组,其余四块分别喷施实施例1-3和对比例中的水溶肥料,并将其记作为实施例1、实施例2、实施例3和对比例,对不同试验田的番茄产量进行记录,记录数据如下表所示:Randomly divide 4 test fields of 3 meters × 10 meters in the test field, and plant tomatoes of the same variety according to the same planting method, keep a piece of test field without spraying fertilizer and record it as a blank group, and the remaining four blocks are sprayed with Example 1- 3 and the water-soluble fertilizer in the comparative example, and it is recorded as embodiment 1, embodiment 2, embodiment 3 and comparative example, the tomato output of different experimental fields is recorded, and the record data is shown in the following table:
通过上表的数据显示可知,试验田施例1-3的番茄亩产量明显高于对比例和空白组的亩产量,从而表示本发明实施例1-3生产的含Gly水溶肥料有助于提高农作物的产量;因此,本发明制得的含Gly水溶肥料具有更好的应用前景和市场推广价值。Shown by the data in the table above, it can be known that the yield per mu of tomato in Experimental Field Example 1-3 is significantly higher than that of comparative example and blank group, thereby showing that the Gly-containing water-soluble fertilizer produced by Embodiment 1-3 of the present invention helps to improve crops Therefore, the Gly-containing water-soluble fertilizer prepared by the present invention has better application prospects and market promotion value.
需要说明的是,在本文中,诸如第一和第二等之类的关系术语仅仅用来将一个实体或者操作与另一个实体或操作区分开来,而不一定要求或者暗示这些实体或操作之间存在任何这种实际的关系或者顺序。而且,术语“包括”、“包含”或者其任何其他变体意在涵盖非排他性的包含,从而使得包括一系列要素的过程、方法、物品或者设备不仅包括那些要素,而且还包括没有明确列出的其他要素,或者是还包括为这种过程、方法、物品或者设备所固有的要素。在没有更多限制的情况下,由语句“包括一个……”限定的要素,并不排除在包括所述要素的过程、方法、物品或者设备中还存在另外的相同要素。It should be noted that in this article, relational terms such as first and second are only used to distinguish one entity or operation from another entity or operation, and do not necessarily require or imply that there is a relationship between these entities or operations. There is no such actual relationship or order between them. Furthermore, the term "comprises", "comprises" or any other variation thereof is intended to cover a non-exclusive inclusion such that a process, method, article or apparatus comprising a set of elements includes not only those elements, but also includes elements not expressly listed. other elements of or also include elements inherent in such a process, method, article, or device. Without further limitations, an element defined by the phrase "comprising a ..." does not exclude the presence of additional identical elements in the process, method, article or apparatus comprising said element.
以上实施例仅用以说明本发明的技术方案,而非对其限制;尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:其依然可以对前述各实施例所记载的技术方案进行修改,或者对其中部分技术特征进行等同替换;而这些修改或者替换,并不使相应技术方案的本质脱离本发明各实施例技术方案的精神和范围。The above embodiments are only used to illustrate the technical solutions of the present invention, rather than to limit them; although the present invention has been described in detail with reference to the foregoing embodiments, those of ordinary skill in the art should understand that: it can still be described in the foregoing embodiments Modifications are made to the recorded technical solutions, or equivalent replacements are made to some of the technical features; and these modifications or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present invention.
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