CN107162843A - The method that hot pickled mustard tube special fertilizer is produced with phosphate ore flotation tailings - Google Patents
The method that hot pickled mustard tube special fertilizer is produced with phosphate ore flotation tailings Download PDFInfo
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- CN107162843A CN107162843A CN201710278983.9A CN201710278983A CN107162843A CN 107162843 A CN107162843 A CN 107162843A CN 201710278983 A CN201710278983 A CN 201710278983A CN 107162843 A CN107162843 A CN 107162843A
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- 239000003337 fertilizer Substances 0.000 title claims abstract description 63
- 241000219198 Brassica Species 0.000 title claims abstract description 46
- 235000003351 Brassica cretica Nutrition 0.000 title claims abstract description 29
- 235000003343 Brassica rupestris Nutrition 0.000 title claims abstract description 29
- QKSKPIVNLNLAAV-UHFFFAOYSA-N bis(2-chloroethyl) sulfide Chemical compound ClCCSCCCl QKSKPIVNLNLAAV-UHFFFAOYSA-N 0.000 title claims abstract description 29
- 235000010460 mustard Nutrition 0.000 title claims abstract description 29
- 238000005188 flotation Methods 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title claims abstract description 19
- 229910019142 PO4 Inorganic materials 0.000 title claims abstract description 16
- NBIIXXVUZAFLBC-UHFFFAOYSA-K phosphate Chemical compound [O-]P([O-])([O-])=O NBIIXXVUZAFLBC-UHFFFAOYSA-K 0.000 title claims abstract description 16
- 239000010452 phosphate Substances 0.000 title claims abstract description 16
- 239000002367 phosphate rock Substances 0.000 claims abstract description 26
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 14
- 239000002002 slurry Substances 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000000706 filtrate Substances 0.000 claims abstract description 11
- 229910017604 nitric acid Inorganic materials 0.000 claims abstract description 11
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 11
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000011574 phosphorus Substances 0.000 claims abstract description 9
- 239000011591 potassium Substances 0.000 claims abstract description 9
- 229910052700 potassium Inorganic materials 0.000 claims abstract description 9
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000004202 carbamide Substances 0.000 claims abstract description 7
- WCUXLLCKKVVCTQ-UHFFFAOYSA-M Potassium chloride Chemical compound [Cl-].[K+] WCUXLLCKKVVCTQ-UHFFFAOYSA-M 0.000 claims description 22
- FGIUAXJPYTZDNR-UHFFFAOYSA-N potassium nitrate Chemical compound [K+].[O-][N+]([O-])=O FGIUAXJPYTZDNR-UHFFFAOYSA-N 0.000 claims description 18
- 239000002686 phosphate fertilizer Substances 0.000 claims description 11
- 239000001103 potassium chloride Substances 0.000 claims description 11
- 235000011164 potassium chloride Nutrition 0.000 claims description 11
- 239000004323 potassium nitrate Substances 0.000 claims description 8
- 235000010333 potassium nitrate Nutrition 0.000 claims description 8
- 238000006243 chemical reaction Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 6
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical group C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 claims description 5
- 238000001035 drying Methods 0.000 claims description 5
- 239000004021 humic acid Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 238000005469 granulation Methods 0.000 claims description 4
- 230000003179 granulation Effects 0.000 claims description 4
- 238000006386 neutralization reaction Methods 0.000 claims description 4
- 239000005416 organic matter Substances 0.000 claims description 4
- 102000004196 processed proteins & peptides Human genes 0.000 claims description 4
- 108090000765 processed proteins & peptides Proteins 0.000 claims description 4
- 238000003756 stirring Methods 0.000 claims description 4
- 229920001184 polypeptide Polymers 0.000 claims description 3
- 229910002651 NO3 Inorganic materials 0.000 claims description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 2
- SNRUBQQJIBEYMU-UHFFFAOYSA-N dodecane Chemical compound CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 claims 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims 1
- DBMJMQXJHONAFJ-UHFFFAOYSA-M Sodium laurylsulphate Chemical compound [Na+].CCCCCCCCCCCCOS([O-])(=O)=O DBMJMQXJHONAFJ-UHFFFAOYSA-M 0.000 claims 1
- 235000010855 food raising agent Nutrition 0.000 claims 1
- 229940072033 potash Drugs 0.000 claims 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims 1
- 235000015320 potassium carbonate Nutrition 0.000 claims 1
- MZSDGDXXBZSFTG-UHFFFAOYSA-M sodium;benzenesulfonate Chemical compound [Na+].[O-]S(=O)(=O)C1=CC=CC=C1 MZSDGDXXBZSFTG-UHFFFAOYSA-M 0.000 claims 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 abstract description 10
- YIXJRHPUWRPCBB-UHFFFAOYSA-N magnesium nitrate Chemical compound [Mg+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O YIXJRHPUWRPCBB-UHFFFAOYSA-N 0.000 abstract description 10
- 239000000843 powder Substances 0.000 abstract description 10
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 abstract description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 7
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 6
- 238000004519 manufacturing process Methods 0.000 abstract description 6
- 239000004254 Ammonium phosphate Substances 0.000 abstract description 5
- 229910000147 aluminium phosphate Inorganic materials 0.000 abstract description 5
- 229910000148 ammonium phosphate Inorganic materials 0.000 abstract description 5
- 235000019289 ammonium phosphates Nutrition 0.000 abstract description 5
- 239000011575 calcium Substances 0.000 abstract description 5
- 229910052791 calcium Inorganic materials 0.000 abstract description 5
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 abstract description 5
- 150000002500 ions Chemical class 0.000 abstract description 5
- 239000000395 magnesium oxide Substances 0.000 abstract description 5
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 abstract description 5
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 abstract description 5
- DLYUQMMRRRQYAE-UHFFFAOYSA-N phosphorus pentoxide Inorganic materials O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 abstract description 5
- 230000000717 retained effect Effects 0.000 abstract description 5
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 abstract description 4
- ZCCIPPOKBCJFDN-UHFFFAOYSA-N calcium nitrate Chemical compound [Ca+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O ZCCIPPOKBCJFDN-UHFFFAOYSA-N 0.000 abstract description 4
- MVFCKEFYUDZOCX-UHFFFAOYSA-N iron(2+);dinitrate Chemical compound [Fe+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MVFCKEFYUDZOCX-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 3
- 239000000047 product Substances 0.000 abstract description 3
- OBYUWBOIIKWGJI-UHFFFAOYSA-N [P].O[N+]([O-])=O Chemical compound [P].O[N+]([O-])=O OBYUWBOIIKWGJI-UHFFFAOYSA-N 0.000 abstract 1
- 239000008187 granular material Substances 0.000 abstract 1
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract 1
- GVALZJMUIHGIMD-UHFFFAOYSA-H magnesium phosphate Chemical compound [Mg+2].[Mg+2].[Mg+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O GVALZJMUIHGIMD-UHFFFAOYSA-H 0.000 abstract 1
- 239000004137 magnesium phosphate Substances 0.000 abstract 1
- 229960002261 magnesium phosphate Drugs 0.000 abstract 1
- 229910000157 magnesium phosphate Inorganic materials 0.000 abstract 1
- 235000010994 magnesium phosphates Nutrition 0.000 abstract 1
- 239000011707 mineral Substances 0.000 abstract 1
- 238000012360 testing method Methods 0.000 description 14
- 230000000052 comparative effect Effects 0.000 description 10
- 230000004913 activation Effects 0.000 description 5
- 238000007796 conventional method Methods 0.000 description 4
- YWEUIGNSBFLMFL-UHFFFAOYSA-N diphosphonate Chemical compound O=P(=O)OP(=O)=O YWEUIGNSBFLMFL-UHFFFAOYSA-N 0.000 description 4
- GVGUFUZHNYFZLC-UHFFFAOYSA-N dodecyl benzenesulfonate;sodium Chemical compound [Na].CCCCCCCCCCCCOS(=O)(=O)C1=CC=CC=C1 GVGUFUZHNYFZLC-UHFFFAOYSA-N 0.000 description 4
- 229940080264 sodium dodecylbenzenesulfonate Drugs 0.000 description 4
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 4
- DAJSVUQLFFJUSX-UHFFFAOYSA-M sodium;dodecane-1-sulfonate Chemical compound [Na+].CCCCCCCCCCCCS([O-])(=O)=O DAJSVUQLFFJUSX-UHFFFAOYSA-M 0.000 description 4
- 230000004083 survival effect Effects 0.000 description 4
- MMDJDBSEMBIJBB-UHFFFAOYSA-N [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] Chemical compound [O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[NH6+3] MMDJDBSEMBIJBB-UHFFFAOYSA-N 0.000 description 3
- 239000004067 bulking agent Substances 0.000 description 3
- VXAPDXVBDZRZKP-UHFFFAOYSA-N nitric acid phosphoric acid Chemical class O[N+]([O-])=O.OP(O)(O)=O VXAPDXVBDZRZKP-UHFFFAOYSA-N 0.000 description 3
- 239000013589 supplement Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000003213 activating effect Effects 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- MXZRMHIULZDAKC-UHFFFAOYSA-L ammonium magnesium phosphate Chemical compound [NH4+].[Mg+2].[O-]P([O-])([O-])=O MXZRMHIULZDAKC-UHFFFAOYSA-L 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 2
- VCJMYUPGQJHHFU-UHFFFAOYSA-N iron(3+);trinitrate Chemical compound [Fe+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VCJMYUPGQJHHFU-UHFFFAOYSA-N 0.000 description 2
- 239000011777 magnesium Substances 0.000 description 2
- 229910052749 magnesium Inorganic materials 0.000 description 2
- 229910000402 monopotassium phosphate Inorganic materials 0.000 description 2
- 235000019796 monopotassium phosphate Nutrition 0.000 description 2
- PJNZPQUBCPKICU-UHFFFAOYSA-N phosphoric acid;potassium Chemical compound [K].OP(O)(O)=O PJNZPQUBCPKICU-UHFFFAOYSA-N 0.000 description 2
- 235000021110 pickles Nutrition 0.000 description 2
- 238000001556 precipitation Methods 0.000 description 2
- 235000010344 sodium nitrate Nutrition 0.000 description 2
- 239000004317 sodium nitrate Substances 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-N Fluorane Chemical compound F KRHYYFGTRYWZRS-UHFFFAOYSA-N 0.000 description 1
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 description 1
- 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 1
- 238000010521 absorption reaction Methods 0.000 description 1
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 238000005056 compaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 229910000040 hydrogen fluoride Inorganic materials 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 239000000618 nitrogen fertilizer Substances 0.000 description 1
- NDLPOXTZKUMGOV-UHFFFAOYSA-N oxo(oxoferriooxy)iron hydrate Chemical compound O.O=[Fe]O[Fe]=O NDLPOXTZKUMGOV-UHFFFAOYSA-N 0.000 description 1
- OJMIONKXNSYLSR-UHFFFAOYSA-N phosphorous acid Chemical compound OP(O)O OJMIONKXNSYLSR-UHFFFAOYSA-N 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910052567 struvite Inorganic materials 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000000844 transformation Methods 0.000 description 1
Classifications
-
- 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
- C05G3/80—Soil conditioners
-
- C—CHEMISTRY; METALLURGY
- C05—FERTILISERS; MANUFACTURE THEREOF
- C05B—PHOSPHATIC FERTILISERS
- C05B7/00—Fertilisers based essentially on alkali or ammonium orthophosphates
-
- 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
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Pest Control & Pesticides (AREA)
- Soil Sciences (AREA)
- Fertilizers (AREA)
Abstract
本发明公开一种用磷矿浮选尾矿生产榨菜专用肥的方法,按质量份数计算,将80‑120份磷矿浮选尾矿,160‑200份磷矿粉和200‑250份水加入到反应器内混匀后,加入200‑250份硝酸反应5‑10min后过滤保留滤液,接着向滤液中加入150‑180份钾肥,130‑160份尿素,20‑30份磷铵以及18‑22份活化疏松剂待其溶解后再加入170‑200份氨气中和得到磷肥料浆,将磷肥料浆造粒或烘干得到硝酸磷肥,本发明通过硝酸分解磷矿浮选尾矿和磷矿粉中的五氧化二磷、钙、镁氧化物等,生成溶于水的磷酸、硝酸钙、硝酸镁、磷酸镁、硝酸镁、硝酸铁等可溶性成分并最终以离子形式保留在成品中,该方法充分利用了尾矿和磷矿中的所有对作物生长有用的元素,制成的肥料氮、磷、钾配比合理,疏松性好,非常合适种植榨菜。
The invention discloses a method for producing special fertilizer for pickled mustard by using phosphate rock flotation tailings. Calculated by mass, 80-120 parts of phosphate rock flotation tailings, 160-200 parts of phosphate rock powder and 200-250 parts of water After adding into the reactor and mixing well, add 200-250 parts of nitric acid to react for 5-10 minutes, then filter and retain the filtrate, then add 150-180 parts of potassium fertilizer, 130-160 parts of urea, 20-30 parts of ammonium phosphate and 18-18 parts of After 22 parts of activated loosening agent is dissolved, add 170-200 parts of ammonia gas to neutralize to obtain phosphorus fertilizer slurry, and granulate or dry the phosphorus fertilizer slurry to obtain nitrophosphate fertilizer. The present invention decomposes phosphate ore flotation tailings and phosphorus by nitric acid Phosphorus pentoxide, calcium, magnesium oxide, etc. in the mineral powder generate water-soluble phosphoric acid, calcium nitrate, magnesium nitrate, magnesium phosphate, magnesium nitrate, iron nitrate and other soluble components, which are finally retained in the finished product in the form of ions. The method makes full use of all the elements useful for crop growth in the tailings and phosphate rock, and the fertilizer produced has a reasonable ratio of nitrogen, phosphorus and potassium and good porosity, and is very suitable for planting mustard.
Description
技术领域technical field
本发明涉及工业固废无害化处置及资源化利用技术领域,具体涉及一种用磷矿浮选尾矿生产榨菜专用肥的方法。The invention relates to the technical field of harmless disposal and resource utilization of industrial solid waste, in particular to a method for producing special fertilizer for pickled mustard by using phosphorite flotation tailings.
背景技术Background technique
随着湿法磷酸工业的快速发展,国内磷矿行业产生了大量中低品位浮选磷矿尾矿,这些尾矿长期堆存,不仅占用大量土地资源,而且存在尾矿库的安全风险,研究这些固体工业废弃物的资源化利用具有十分重要的意义。With the rapid development of the wet-process phosphoric acid industry, the domestic phosphate rock industry has produced a large number of low- and medium-grade flotation phosphate rock tailings. These tailings have been stockpiled for a long time, which not only occupies a large amount of land resources, but also poses safety risks for tailings ponds. Research The resource utilization of these solid industrial wastes is of great significance.
榨菜为芥菜的变种,芥菜常用于腌制咸酸菜,其肉质茎髓是重庆榨菜原料,属于十字花科、芸薹属。作为重庆涪陵地区特色作物种植面积高达百万亩,榨菜对肥料需量大,基肥要求高,生长期间还要分期追肥;因此需要一种能够满足榨菜用肥的专用肥。Mustard mustard is a variant of mustard. Mustard is often used to pickle pickles. As a specialty crop in the Fuling area of Chongqing, the planting area is as high as one million mu. Mustard mustard has a large demand for fertilizers, high requirements for base fertilizer, and topdressing in stages during the growth period; therefore, a special fertilizer that can meet the needs of mustard mustard is needed.
发明内容Contents of the invention
为解决以上技术问题,本发明提供一种工艺简单的磷矿浮选尾矿生产榨菜专用肥的方法。In order to solve the above technical problems, the present invention provides a method for producing special fertilizer for pickled mustard with simple process from phosphate ore flotation tailings.
技术方案如下:一种用磷矿浮选尾矿生产榨菜专用肥的方法,其关键在于按以下步骤进行:The technical scheme is as follows: a method for producing special fertilizer for pickled mustard with phosphate ore flotation tailings, the key of which is to carry out according to the following steps:
步骤(1):将80-120份磷矿浮选尾矿,160-200份磷矿粉以及200-250份水加入到反应器内,充分混合并搅拌均匀,然后向反应器中加入200-250份硝酸,反应5-10min后过滤,保留滤液;Step (1): Add 80-120 parts of phosphate rock flotation tailings, 160-200 parts of phosphate rock powder and 200-250 parts of water into the reactor, mix well and stir evenly, and then add 200- 250 parts of nitric acid, filter after reacting for 5-10 minutes, and keep the filtrate;
步骤(2):向滤液中加入150-180份钾肥,130-160份尿素,20-30份磷铵以及18-22份活化疏松剂待其充分溶解;Step (2): Add 150-180 parts of potassium fertilizer, 130-160 parts of urea, 20-30 parts of ammonium phosphate and 18-22 parts of activated loosening agent to the filtrate until it is fully dissolved;
步骤(3):溶解后再加入170-200份氨气进行中和反应,控制反应后物料的 pH值为5.0-6.0得到磷肥料浆;Step (3): after dissolving, add 170-200 parts of ammonia gas to carry out neutralization reaction, control the pH value of the material after the reaction to be 5.0-6.0 to obtain phosphorus fertilizer slurry;
步骤(4):将所述磷肥料浆浓缩造粒或烘干得到硝酸磷肥;Step (4): Concentrating, granulating or drying the phosphate fertilizer slurry to obtain nitrophosphate fertilizer;
以上各成分均按质量份数计算。Each of the above components is calculated in parts by mass.
采用上述技术方案利用硝酸分解磷矿浮选尾矿和磷矿粉中的五氧化二磷、钙、镁氧化物等,生成溶于水的磷酸、硝酸钙、硝酸镁、磷酸铵镁、硝酸镁、硝酸铁等可溶性成分并最终以离子形式保留在成品中,是作物生长必须的元素;而磷矿粉中的氟则以氟化氢气体的形式排出、二氧化硅以沉淀形式经过滤可回收另做他用,该方法可完全利用尾矿和磷矿中的所有对作物生长有用的元素,而传统的采用硫酸分解的方式会产生硫酸钙沉淀,钙元素被过滤排出,制成的肥料中缺乏作物生长必须的钙元素,其他有用元素未得到充分运用。Using the above technical scheme, use nitric acid to decompose phosphorus pentoxide, calcium, magnesium oxide, etc. in phosphate rock flotation tailings and phosphate rock powder, and generate phosphoric acid, calcium nitrate, magnesium nitrate, magnesium ammonium phosphate, and magnesium nitrate that are soluble in water Soluble components such as ferric nitrate and iron nitrate are finally retained in the finished product in the form of ions, which are essential elements for crop growth; while the fluorine in the rock phosphate powder is discharged in the form of hydrogen fluoride gas, and the silica is recovered in the form of precipitation after filtration. He said that this method can fully utilize all the elements useful for crop growth in the tailings and phosphate rock, while the traditional method of sulfuric acid decomposition will produce calcium sulfate precipitation, the calcium element is filtered out, and the fertilizer produced lacks crops Calcium is necessary for growth, and other useful elements are not fully utilized.
作为优选:所述硝酸磷肥中N:P:K的质量比为20:8:10。Preferably: the mass ratio of N:P:K in the nitrophosphate fertilizer is 20:8:10.
按质量百分比计算,所述活化疏松剂由8-9%的有机质,0.5%的硝酸盐, 7.5-7.9%的十二烷基苯磺酸钠,0.3-0.4%的十二烷基磺酸钠,0.4-0.6%的OP-10, 0.4-0.6%的KCl以及余量的水组成。Calculated by mass percentage, the activated loosening agent consists of 8-9% organic matter, 0.5% nitrate, 7.5-7.9% sodium dodecylbenzenesulfonate, and 0.3-0.4% sodium dodecylsulfonate , 0.4-0.6% of OP-10, 0.4-0.6% of KCl and the balance of water.
上述有机质为腐殖酸或多肽。采用此方案腐殖酸和多肽不仅有很好的改善土壤板结的效果,同时还能给作物补充有机肥。The above organic matter is humic acid or polypeptide. The use of humic acid and peptides in this solution not only has a good effect on improving soil compaction, but also supplements organic fertilizers to crops.
上述硝酸的浓度为65-68%。The concentration of above-mentioned nitric acid is 65-68%.
上述钾肥为氯化钾或硝酸钾。采用此设计硝酸分解磷矿粉生成磷酸和硝酸的混酸,该混酸和氯化钾或硝酸钾反应生成磷酸二氢钾和硝酸钾,补充肥料中的钾元素,而钾元素也是作物生长的必须元素之一。Above-mentioned potassium fertilizer is potassium chloride or potassium nitrate. Using this design, nitric acid decomposes phosphate rock powder to generate a mixed acid of phosphoric acid and nitric acid. The mixed acid reacts with potassium chloride or potassium nitrate to generate potassium dihydrogen phosphate and potassium nitrate, which supplements the potassium element in the fertilizer, and potassium element is also an essential element for crop growth. one.
步骤(4)中所述造粒方法为喷浆造粒;所述烘干为在100-105℃下烘干。The granulation method in step (4) is spray granulation; the drying is drying at 100-105°C.
磷矿粉中含与28.91%的五氧化二磷、5.10%的氧化镁、0.61%的三氧化二铁,其中的P、Mg和Fe最终都以离子形式保留在肥料中;磷矿浮选尾矿中还有6.06%的五氧化二磷、33.51%的氧化钙、17.2%的氧化镁,其中的P、Ca、Mg均以可溶性离子形式保留在肥料中,是作物生长的必须元素。Phosphate rock powder contains 28.91% of phosphorus pentoxide, 5.10% of magnesium oxide, and 0.61% of ferric oxide, among which P, Mg and Fe are finally retained in the fertilizer in the form of ions; phosphate rock flotation tailings There are also 6.06% phosphorus pentoxide, 33.51% calcium oxide, and 17.2% magnesium oxide in the mine, among which P, Ca, and Mg are all retained in the fertilizer in the form of soluble ions, which are essential elements for crop growth.
有益效果:采用本发明的有益效果是通过硝酸分解磷矿浮选尾矿和磷矿粉中的五氧化二磷、钙、镁氧化物等,生成溶于水的磷酸、硝酸钙、硝酸镁、磷酸铵镁、硝酸镁、硝酸铁等可溶性成分并最终以离子形式保留在成品中,而磷酸和硝酸的混酸又会与氯化钾或硝酸钾反应生成磷酸二氢钾和硝酸钾,补充肥料中的钾元素,中和用的氨气同时也作为氮肥来源补充肥料的氮元素,该方法充分利用了尾矿和磷矿中的所有对作物生长有用的元素,制成的肥料氮、磷、钾配比合理,疏松性好,非常合适种植榨菜。Beneficial effect: the beneficial effect of adopting the present invention is to decompose phosphorus pentoxide, calcium, magnesium oxide, etc. Ammonium magnesium phosphate, magnesium nitrate, iron nitrate and other soluble components are finally retained in the finished product in the form of ions, while the mixed acid of phosphoric acid and nitric acid will react with potassium chloride or potassium nitrate to form potassium dihydrogen phosphate and potassium nitrate, which can be added to the fertilizer The potassium element used for neutralization is also used as a source of nitrogen fertilizer to supplement the nitrogen element of the fertilizer. This method makes full use of all the elements useful for crop growth in the tailings and phosphate rock, and the fertilizer nitrogen, phosphorus, and potassium The ratio is reasonable, the porosity is good, and it is very suitable for growing mustard.
附图说明Description of drawings
图1为实施例3中硝酸磷肥的疏松性照片;Fig. 1 is the loose photo of nitrophosphate fertilizer in embodiment 3;
图2为对比试验例1的中肥料的疏松性照片。Fig. 2 is a photograph of the looseness of the fertilizer in comparative test example 1.
具体实施方式detailed description
下面结合实施例和附图对本发明作进一步说明。The present invention will be further described below in conjunction with the embodiments and accompanying drawings.
实施例1,一种用磷矿浮选尾矿生产榨菜专用肥的方法,按以下步骤进行:首先配置活化疏松剂,按质量百分比计算,将8%的腐殖酸,0.5%的硝酸钾,7.5%的十二烷基苯磺酸钠,0.3%的十二烷基磺酸钠,0.4%的OP-10,0.4%的KCl以及余量的水混合均匀得到所述活化疏松剂;Embodiment 1, a kind of method for producing mustard special fertilizer with phosphate ore flotation tailings, carries out as follows: first configure activation bulking agent, calculate by mass percentage, with 8% humic acid, 0.5% potassium nitrate, 7.5% sodium dodecylbenzene sulfonate, 0.3% sodium dodecyl sulfonate, 0.4% OP-10, 0.4% KCl and the rest of the water are mixed uniformly to obtain the activated loosening agent;
按质量份数计算,将80份磷矿浮选尾矿,160份磷矿粉以及200份水加入到反应器内,充分混合并搅拌均匀,然后向反应器中加入200份浓度为65%硝酸,反应5min后过滤,保留滤液,接着向滤液中加入150份硝酸钾,130份尿素,20份磷铵以及18份活化疏松剂待其充分溶解,溶解后再加入170份氨气进行中和反应,控制反应后物料的pH值为5.0得到磷肥料浆,将所述磷肥料浆浓缩喷浆造粒得到高硝态氮含量的硝酸磷肥,该硝酸磷肥中N:P:K的质量比为 20:8:10。Calculated in parts by mass, add 80 parts of phosphate rock flotation tailings, 160 parts of phosphate rock powder and 200 parts of water into the reactor, fully mix and stir evenly, and then add 200 parts of 65% nitric acid into the reactor , filter after reacting for 5 minutes, retain the filtrate, then add 150 parts of potassium nitrate, 130 parts of urea, 20 parts of ammonium phosphate and 18 parts of activated loosening agent to the filtrate until it is fully dissolved, and then add 170 parts of ammonia for neutralization reaction , the pH value of the material after the control reaction is 5.0 to obtain phosphorus fertilizer slurry, and the nitrophosphate fertilizer with high nitrate nitrogen content is obtained by concentrated spraying and granulation of the phosphorus fertilizer slurry, and the mass ratio of N:P:K in this nitrate phosphate fertilizer is 20 :8:10.
按常规方法种植榨菜,然后在榨菜的成活期按25kg/亩的量施加一次所述硝酸磷肥,并在榨菜的膨大期按20kg/亩的量再次施加一次所述硝酸磷肥。Plant mustard by conventional methods, then apply once described nitrophosphate fertilizer by the amount of 25kg/mu during the survival period of mustard mustard, and apply once again described nitrophosphate fertilizer by the amount of 20kg/mu during the expansion period of mustard mustard.
实施例2,一种用磷矿浮选尾矿生产榨菜专用肥的方法,按以下步骤进行:首先配置活化疏松剂,按质量百分比计算,将9%的多肽,0.5%的硝酸钠,7.9%的十二烷基苯磺酸钠,0.4%的十二烷基磺酸钠,0.6%的OP-10,0.6%的KCl以及81.0%的水混合均匀得到所述活化疏松剂;Embodiment 2, a kind of method that uses phosphate ore flotation tailings to produce mustard mustard special fertilizer, carries out according to the following steps: first configure activation loosening agent, calculate by mass percentage, with 9% polypeptide, 0.5% sodium nitrate, 7.9% Sodium dodecylbenzenesulfonate, 0.4% sodium dodecylsulfonate, 0.6% OP-10, 0.6% KCl and 81.0% water are mixed uniformly to obtain the activated loosening agent;
按质量份数计算,将120份磷矿浮选尾矿,200份磷矿粉以及250份水加入到反应器内,充分混合并搅拌均匀,然后向反应器中加入250份浓度为68%的硝酸,反应10min后过滤,保留滤液,接着向滤液中加入180份氯化钾,160 份尿素,30份磷铵以及22份活化疏松剂待其充分溶解,溶解后再加入200份氨气进行中和反应,控制反应后物料的pH值为6.0得到磷肥料浆,将所述磷肥料浆在100℃下烘干、粉碎得到高硝态氮含量的硝酸磷肥,该硝酸磷肥中N:P:K的质量比为20:8:10。Calculated in parts by mass, 120 parts of phosphate rock flotation tailings, 200 parts of phosphate rock powder and 250 parts of water are added to the reactor, fully mixed and stirred evenly, and then 250 parts of phosphate rock with a concentration of 68% are added to the reactor Nitric acid, filter after reacting for 10 minutes, keep the filtrate, then add 180 parts of potassium chloride, 160 parts of urea, 30 parts of ammonium phosphate and 22 parts of activating loosening agent to the filtrate until it is fully dissolved, then add 200 parts of ammonia gas to proceed and reaction, the pH value of the material after the reaction is controlled to be 6.0 to obtain a phosphate fertilizer slurry, and the phosphate fertilizer slurry is dried and pulverized at 100° C. to obtain a nitrophosphate fertilizer with a high nitrate nitrogen content. In this nitrate phosphate fertilizer, N:P:K The mass ratio is 20:8:10.
按常规方法种植榨菜,然后在榨菜的成活期按25kg/亩的量施加一次所述硝酸磷肥,并在榨菜的膨大期按20kg/亩的量再次施加一次所述硝酸磷肥。Plant mustard by conventional methods, then apply once described nitrophosphate fertilizer by the amount of 25kg/mu during the survival period of mustard mustard, and apply once again described nitrophosphate fertilizer by the amount of 20kg/mu during the expansion period of mustard mustard.
实施例3,一种用磷矿浮选尾矿生产榨菜专用肥的方法,按以下步骤进行:首先配置活化疏松剂,按质量百分比计算,将8.5%的腐殖酸,0.5%的硝酸钠, 7.7%的十二烷基苯磺酸钠,0.35%的十二烷基磺酸钠,0.5%的OP-10(即辛烷基苯酚-10),0.5%的KCl以及82.0%的水混合均匀得到所述活化疏松剂;Embodiment 3, a kind of method that uses phosphate ore flotation tailings to produce mustard mustard special fertilizer, carries out as follows: first configure activation loosening agent, calculate by mass percentage, with 8.5% humic acid, 0.5% sodium nitrate, 7.7% sodium dodecylbenzene sulfonate, 0.35% sodium dodecyl sulfonate, 0.5% OP-10 (that is, octylphenol-10), 0.5% KCl and 82.0% water mix well obtain the activated loosening agent;
按质量份数计算,将100份磷矿浮选尾矿,180份磷矿粉以及220份水加入到反应器内,充分混合并搅拌均匀,然后向反应器中加入234份浓度为66%的硝酸,反应8min后过滤,保留滤液,接着向滤液中加入168份氯化钾,145份尿素,24份磷铵以及20份活化疏松剂待其充分溶解,溶解后再加入182份氨气进行中和反应,控制反应后物料的pH值为5.5得到磷肥料浆,将所述磷肥料浆在105℃下烘干、粉碎得到高硝态氮含量的硝酸磷肥,该硝酸磷肥中N:P:K的质量比为20:8:10。Calculated in parts by mass, add 100 parts of phosphate rock flotation tailings, 180 parts of phosphate rock powder and 220 parts of water into the reactor, fully mix and stir evenly, and then add 234 parts of phosphate rock with a concentration of 66% into the reactor Nitric acid, filter after reacting for 8 minutes, keep the filtrate, then add 168 parts of potassium chloride, 145 parts of urea, 24 parts of ammonium phosphate and 20 parts of activating loosening agent to the filtrate until it is fully dissolved, then add 182 parts of ammonia to carry out and reaction, the pH value of the material after the reaction is controlled to be 5.5 to obtain a phosphate fertilizer slurry, and the phosphate fertilizer slurry is dried and pulverized at 105° C. to obtain a nitrophosphate fertilizer with a high nitrate nitrogen content. In this nitrate phosphate fertilizer, N:P:K The mass ratio is 20:8:10.
按常规方法种植榨菜,然后在榨菜的成活期按25kg/亩的量施加一次所述硝酸磷肥,并在榨菜的膨大期按20kg/亩的量再次施加一次所述硝酸磷肥。Plant mustard by conventional methods, then apply once described nitrophosphate fertilizer by the amount of 25kg/mu during the survival period of mustard mustard, and apply once again described nitrophosphate fertilizer by the amount of 20kg/mu during the expansion period of mustard mustard.
对比试验例1,该对比试验例与实施例3的不同之处在于,制备的过程中未加入活化疏松剂。Comparative Test Example 1, the difference between this Comparative Test Example and Example 3 is that no activation loosening agent is added during the preparation process.
对比试验例2,按常规方法种植榨菜,在榨菜的成活期按43kg/亩的量施加一次市售腾升复合肥(其中N:P:K比例为15:15:15),并在榨菜的膨大期按20kg/ 亩的量追加尿素。Contrast test example 2, plant mustard by conventional methods, apply once commercially available Tengsheng compound fertilizer (wherein N:P:K ratio is 15:15:15) by the amount of 43kg/mu in the survival period of mustard, and in mustard mustard During the expansion period, add urea at an amount of 20kg/mu.
下面结合试验和试验数据进一步说明本发明。Below in conjunction with test and test data further illustrate the present invention.
1、疏松性对比:图1为实施例3制备的硝酸磷肥疏松性照片;图2为对比试验例1制备的肥料的疏松性照片;从图1和图2的对比可以看出,加入了活化疏松剂的实施例3制备的硝酸磷肥的分散性较好,而未加入活化疏松剂的对比试验例1的肥料呈块状,疏松性差。1. Contrast of porosity: Fig. 1 is a photo of the porosity of the nitrophosphate fertilizer prepared in Example 3; Fig. 2 is a photo of the porosity of the fertilizer prepared in Comparative Test Example 1; as can be seen from the comparison of Fig. 1 and Fig. 2, the addition of activation The nitrophosphate fertilizer prepared in Example 3 of the bulking agent had better dispersibility, while the fertilizer in Comparative Test Example 1 without adding the activated bulking agent was lumpy and poor in bulk.
2、分别取实施例1、实施例2和实施例3种植的榨菜以及对比试验例1和对比试验例2种植的榨菜进行对比,结果如表1所示。2. The pickled mustard planted in Example 1, Example 2 and Example 3 and the mustard planted in Comparative Test Example 1 and Comparative Test Example 2 were compared respectively, and the results are shown in Table 1.
表1 产量对比Table 1 Yield comparison
从上表可以看出,实施例1-3的榨菜亩产量和单个榨菜的重量均显著高于对比试验例2的亩产量和单个重量,由此可见采用本发明提供的方法制备的硝酸磷肥与现有的普通肥料相比更合适榨菜生长;从上表还可以看出对比试验例1 中种植的榨菜的亩产量和单个重量较对比试验例2相比均有所上升,但略低于实施例1-3的榨菜亩产量和单个榨菜的重量,这主要是由于对比试验例1中制备的肥料中没有添加活化疏松剂,制备的肥料疏松性较差且缺乏有机质,作物吸收利用率低,因此种植的榨菜的亩产量和单个重量均略低。As can be seen from the above table, the yield per mu of mustard tuber and the weight of a single mustard tuber of embodiment 1-3 are all significantly higher than the yield per mu and the single weight of comparative test example 2, thus it can be seen that the nitrophosphate fertilizer prepared by the method provided by the invention is compatible with Existing common fertilizer is more suitable for mustard mustard growth; From the above table, it can also be seen that the yield per mu of mustard planted in comparative test example 1 and the single weight comparison test example 2 all increase, but slightly lower than the implementation The mustard yield per mu of example 1-3 and the weight of a single mustard, this is mainly due to not adding activated loosening agent in the fertilizer prepared in comparative test example 1, the fertilizer porosity prepared is poor and lacks organic matter, and the crop absorption utilization rate is low, Therefore, the yield per mu and the individual weight of the mustard planted are slightly lower.
综上所述,本发明提供的用磷矿浮选尾矿生产榨菜专用肥的方法制备的硝酸磷肥非常适合榨菜生长,可显著提升榨菜的产量和单个重量。In summary, the nitrophosphate fertilizer prepared by the method for producing mustard special fertilizer from phosphate ore flotation tailings provided by the present invention is very suitable for the growth of mustard, and can significantly increase the yield and individual weight of mustard.
最后需要说明的是,上述描述仅仅为本发明的优选实施例,本领域的普通技术人员在本发明的启示下,在不违背本发明宗旨及权利要求的前提下,可以做出多种类似的表示,这样的变换均落入本发明的保护范围之内。Finally, it should be noted that the above description is only a preferred embodiment of the present invention, and those of ordinary skill in the art can make a variety of similar implementations under the inspiration of the present invention without violating the purpose and claims of the present invention. It means that such transformations all fall within the protection scope of the present invention.
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107903142A (en) * | 2017-12-29 | 2018-04-13 | 中化重庆涪陵化工有限公司 | A kind of Special compound fertilizer for tobacco and the method for preparing the composite fertilizer using phosphate ore flotation tailings |
CN108530207A (en) * | 2018-07-02 | 2018-09-14 | 郑州大学 | A method of preparing particle urea nitro-compound fertilizer with urea decomposing phosphorite by using nitric acid |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU793961A1 (en) * | 1978-08-28 | 1981-01-07 | Киевский Ордена Ленина Политехни-Ческий Институт Им.50-Летия Вели-Кой Октябрьской Социалистическойреволюции | Method of producing complex fertilizers |
CN1240776A (en) * | 1998-06-25 | 2000-01-12 | 郑州工业大学 | Calcium perphosphate fertilizer with shorter ageing time and not blocking and its preparing process |
CN1417108A (en) * | 2002-12-11 | 2003-05-14 | 南化集团研究院 | New calcium superphosphate activating and loosening agent |
CN101451200A (en) * | 2007-11-29 | 2009-06-10 | 北京有色金属研究总院 | Rare-earth enrichment recovery method from phosphorite |
CN103011984A (en) * | 2013-01-04 | 2013-04-03 | 福建省邵武市榕丰化工有限公司 | Liquid superphosphate active porous agent |
CN104876768A (en) * | 2015-05-18 | 2015-09-02 | 金正大诺泰尔化学有限公司 | Soil conditioner prepared by activating phosphate rock tailings by using organic/inorganic activators and preparation method thereof |
CN105776167A (en) * | 2015-04-02 | 2016-07-20 | 贵州芭田生态工程有限公司 | Polyphosphate and preparation method thereof |
CN106315528A (en) * | 2015-06-30 | 2017-01-11 | 铜仁市万山区盛和矿业有限责任公司 | Phosphorite tailing processing and comprehensive utilization method |
-
2017
- 2017-04-25 CN CN201710278983.9A patent/CN107162843A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SU793961A1 (en) * | 1978-08-28 | 1981-01-07 | Киевский Ордена Ленина Политехни-Ческий Институт Им.50-Летия Вели-Кой Октябрьской Социалистическойреволюции | Method of producing complex fertilizers |
CN1240776A (en) * | 1998-06-25 | 2000-01-12 | 郑州工业大学 | Calcium perphosphate fertilizer with shorter ageing time and not blocking and its preparing process |
CN1417108A (en) * | 2002-12-11 | 2003-05-14 | 南化集团研究院 | New calcium superphosphate activating and loosening agent |
CN101451200A (en) * | 2007-11-29 | 2009-06-10 | 北京有色金属研究总院 | Rare-earth enrichment recovery method from phosphorite |
CN103011984A (en) * | 2013-01-04 | 2013-04-03 | 福建省邵武市榕丰化工有限公司 | Liquid superphosphate active porous agent |
CN105776167A (en) * | 2015-04-02 | 2016-07-20 | 贵州芭田生态工程有限公司 | Polyphosphate and preparation method thereof |
CN104876768A (en) * | 2015-05-18 | 2015-09-02 | 金正大诺泰尔化学有限公司 | Soil conditioner prepared by activating phosphate rock tailings by using organic/inorganic activators and preparation method thereof |
CN106315528A (en) * | 2015-06-30 | 2017-01-11 | 铜仁市万山区盛和矿业有限责任公司 | Phosphorite tailing processing and comprehensive utilization method |
Non-Patent Citations (3)
Title |
---|
M.H.纳比耶夫 等: "《硝酸磷肥上册 硝酸处理磷矿的理论基础》", 30 September 1980, 化学工业出版社 * |
李兵 等: "磷矿浮选尾矿制备钙镁复混肥及肥效试验研究", 《磷肥与复肥》 * |
西南农学院土壤农化系农化教研组: "《化肥的合理施用》", 30 June 1979, 四川人民出版社 * |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107903142A (en) * | 2017-12-29 | 2018-04-13 | 中化重庆涪陵化工有限公司 | A kind of Special compound fertilizer for tobacco and the method for preparing the composite fertilizer using phosphate ore flotation tailings |
CN108530207A (en) * | 2018-07-02 | 2018-09-14 | 郑州大学 | A method of preparing particle urea nitro-compound fertilizer with urea decomposing phosphorite by using nitric acid |
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