CN109180277A - A method of Si, Ca, Mg, K fertilizer is produced using rotary kiln calcining serpentine - Google Patents

A method of Si, Ca, Mg, K fertilizer is produced using rotary kiln calcining serpentine Download PDF

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Publication number
CN109180277A
CN109180277A CN201811360575.9A CN201811360575A CN109180277A CN 109180277 A CN109180277 A CN 109180277A CN 201811360575 A CN201811360575 A CN 201811360575A CN 109180277 A CN109180277 A CN 109180277A
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CN
China
Prior art keywords
raw material
serpentine
fertilizer
rotary kiln
cao
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Pending
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CN201811360575.9A
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Chinese (zh)
Inventor
慕湧
俞海明
吴汉元
李秉勃
田淑芳
徐向阳
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Ruoqiang Shengdi Asbestos Tailings Reuse Technology Development Co Ltd
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Ruoqiang Shengdi Asbestos Tailings Reuse Technology Development Co Ltd
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Priority to CN201811360575.9A priority Critical patent/CN109180277A/en
Publication of CN109180277A publication Critical patent/CN109180277A/en
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    • CCHEMISTRY; METALLURGY
    • C05FERTILISERS; MANUFACTURE THEREOF
    • C05DINORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C; FERTILISERS PRODUCING CARBON DIOXIDE
    • C05D1/00Fertilisers containing potassium
    • C05D1/02Manufacture from potassium chloride or sulfate or double or mixed salts thereof
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G37/00Compounds of chromium
    • C01G37/02Oxides or hydrates thereof
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/02Oxides; Hydroxides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/02Oxides; Hydroxides
    • C01G49/06Ferric oxide [Fe2O3]
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G49/00Compounds of iron
    • C01G49/02Oxides; Hydroxides
    • C01G49/08Ferroso-ferric oxide [Fe3O4]
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G51/00Compounds of cobalt
    • C01G51/04Oxides; Hydroxides
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01GCOMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
    • C01G53/00Compounds of nickel
    • C01G53/04Oxides; Hydroxides

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Fertilizers (AREA)

Abstract

The invention discloses a kind of methods using rotary kiln calcining serpentine production Si, Ca, Mg, K fertilizer, include the following steps: 1, roping serpentine, lime stone, potassium chloride raw material to cement producing line;2, prepare it is carbon containing be greater than 80% graphite it is stand-by to the production line;3, by above raw material according to the ratio of mass percent: serpentine: lime stone: potassium chloride: graphitic carbon=63%:28%:6%:3% ratio is added to rotary kiln, calcines in 850~1200 DEG C of temperature ranges, temperature of charge, which reaches 900 DEG C or more, to discharge;4, the material after discharging is milled down to 140 mesh in clinker grinding mill, by magnetic belt separator magnetic separation after discharging, magneticly elects and does not have magnetic material to use as the powder raw material of Si, Ca, Mg, K fertilizer;5, more than chemical examination powder raw material, detects CaO, SiO therein2、K2O, the content of MgO;6, after detecting, CaO insufficient section is supplied, K with desulfurized gypsum2O is insufficient, is supplied by potassium sulfate, and then in pelletizing production line, production becomes pelletized product.

Description

A method of Si, Ca, Mg, K fertilizer is produced using rotary kiln calcining serpentine
Technical field
The present invention relates to a kind of methods using rotary kiln calcining serpentine production Si, Ca, Mg, K fertilizer.
Background technique
The production of minerals fertilizer, most of techniques using calcining.The common raw material of production secondary nutrients has stone Diamond stone, lime stone, dolomite, medical stone, potassium feldspar, vermiculite, oyster shell, coral rock etc..These raw material are substantially to be rich in CaO、SiO2、MgO、K2O etc., the technique of calcining are usually carried out in rotary kiln or shaft furnace.The production of Si, Ca, Mg, K fertilizer is also to use to forge Burning and grinding, the process of granulation.
Searching document discloses: (1), Zhu of HeFei University of Technology announces on there are " stone material " magazine of the 12nd phase in 2000 Entitled " the material composition feature of serpentine and utilization " paper among, have that " serpentine is to insensitive, the hot stability of heat It is good.For the stability of heat, antigorite is higher than lizardite, sharp choysotile.The thermal conductivity of choysotile is no more than 0.23w/ m。
K is good heat-resistant insulation material.The water absorption rate of serpentine is little.This is because serpentine minerals structural unit Interlayer does not adsorb the reason of water.But since the partial size of serpentine is very tiny, or in threadiness, can be inhaled between shred and fiber Attached a small amount of water.Serpentine can do refractory material." content statement;(2) Fu Jiangang, Wang Hui et al. are in 2007 " hydrometallurgys " Among the paper for publishing entitled " development and utilization situation and development trend of serpentine ore " on magazine, there is following content statement: " water soluble phosphorous fertilizer can be manufactured with snake masonry ingredient, the corporate boss using serpentine production calcium magnesium phosphate domestic at present will have Guangxi phosphate fertilizer plant, YUNLAN Phosphor Fertilizer Plant, Donghai Area, Jiangsu phosphate fertilizer plant etc..Its production technology uses smelting process ".
According to above statement it is found that there is presently no the techniques using rotary kiln calcining serpentine production Si, Ca, Mg, K fertilizer. Furthermore as the sylvite base of Largest In China, Lop Nur sylvite can be used as Fertilizer application, but potassium chloride composite fertilizer contains chlorine Height is not applied for the fear-chlorion crops such as tobacco, sugarcane, potato, tealeaves, beet.
Inventor's discovery when studying Ruoqiang county according to the snake stone structure for gulping down the town Bu Lake, serpentine centre are contained The various heavies such as Cr, Pb, Cd, Fe, Co, Mn, Ni, Mo.Wherein the content of Cr has been more than national chemical fertilizer GB/T 23349-2009 " arsenic, cadmium, lead, chromium, mercury ecological index in fertilizer " removes so needing certain technique about using serpentine production fertilizer The ingredient of Cr among serpentine, can meet the use standard of fertilizer, and Xinjiang among the serpentine for gulping down the area Bu Lake according to having The comparison of the ingredient situation and national standard of evil element is as shown in the table:
Summary of the invention
The purpose of the present invention is to provide a kind of method using rotary kiln calcining serpentine production Si, Ca, Mg, K fertilizer, foundations The characteristics of mineralization machanism and mineral tissue of serpentine, using metallurgical transmission theory, in conjunction with heavy metallic oxide reduction reaction Free energy numerical value produces minerals fertilizer by rotary kiln using the method with addition of amount of activated material and reproducibility material, Applied to Agriculture, forestry And Animal Husbandry industry.
The object of the present invention is achieved like this, a kind of side using rotary kiln calcining serpentine production Si, Ca, Mg, K fertilizer Method includes the following steps: 1, roping serpentine, lime stone, potassium chloride raw material to cement producing line, wherein the CaO in lime stone Mass percentage content is at least 50%;2, prepare it is carbon containing be greater than 80% graphite it is stand-by to the production line;It 3, will be above Raw material according to mass percent ratio: serpentine: lime stone: potassium chloride: graphitic carbon=63%:28%:6%:3% ratio be added To rotary kiln, calcined in 850~1200 DEG C of temperature ranges, temperature of charge, which reaches 900 DEG C or more, to discharge;4, after discharging Material is milled down to 140 mesh in clinker grinding mill, and by magnetic belt separator magnetic separation after discharging, it is former as metallurgy to magneticly elect magnetic material Material utilizes, and does not have magnetic material to use as the powder raw material of Si, Ca, Mg, K fertilizer;5, more than chemical examination powder raw material, detects it In CaO, SiO2、K2O, the content of MgO and chromium therein, cadmium, arsenic, lead, mercury;6, after above detection, CaO is insufficient Part is supplied with desulfurized gypsum, K2O is insufficient, is supplied by potassium sulfate, and then in pelletizing production line, production becomes pelletized product ?;7, the dedusting ash of rotary kiln is sold to Lead And Zinc Smelter as lead-zinc smelting raw material.
Technical principle of the invention:
1, it is dehydrated using calcining serpentine, generates free SiO2, promote among the component of serpentine, free silica to The conversion of fertilizer efficiency component, weak magnetic iron hydroxide is to ferromagnetic substance Fe among serpentine3O4The equation of conversion, reaction is as follows:
Mg6[Si4O10](OH)8+Q→3Mg2[SiO4]+SiO2+4H2O(calcined dehydration promotes SiO2Crystal is converted to tetrahedron)
2Fe(OH)3+Q=Fe2O3+3H2O (dehydration of the oxide of iron)
Fe2O3+FeO=Fe3O4(magnetization of di-iron trioxide is reacted)
2, since serpentine thermal conductivity is very poor, dewatered forsterite is a kind of refractory material, and KCl6%, Diversity is added For the eutectic temperature of object at 1250 DEG C, promoting serpentine that local sintering state is presented in calcination temperature section (is not in big face Product melting zone), prevent mixture from gluing kiln, while convenient for the broken processing after mixture kiln discharge, recycling valuable among serpentine Metal.
Mg6[Si4O10](OH)8+8KCl+Q→6MgO·SiO2+3SiO2+4K2O+8HCl (dechlorination reaction of potassium chloride)
3, the decomposition reaction of calcium carbonate, the CO of generation2It can be reacted with graphitic carbon, the reducibility gas CO of generation, promote calcining Oxide in the process is converted to metallic state or lower valency, and calcium oxide and magnesia, silicon dioxde reaction generate low melting point Monticellite is conducive to the magnesia and silica crystal structure among serpentine while promoting serpentine to reduce fusing point Conversion, the formation of fertiliser containing magnesium element oxide magnesium completes in this stage, and reaction equation is as follows:
CaCO3+Q=CaO+CO2
CaO+2MgO·SiO2=CaO·MgO·SiO2+ MgO (generation of low melting point and the generation of free magnesium)
4, be added reducing agent C reduction PbO, be allowed to the separation among raw ore object tissue, into dedusting ash, dedusting ash is as lead zinc Raw materials for metallurgy is sold to Lead And Zinc Smelter.
PbO(l)+C=Pb(g) + CO(g)
ΔG0= 252700-247.92T
It is 746 DEG C from reaction starting temperature known to above formula.
PbO(l)+CO=Pb(g)+CO2(g)
ΔG0=86150-76.92T
It is calculated by above formula and knows that reaction starting temperature is 847 DEG C.
5, calcined mixture carries out ball-milling treatment to 140 mesh, and mixture is low under the action of mechano-chemical reation Melting Substance will be converted to free state substance, further discharge the fertilizer efficiency of sintered state mixture moderate-element, the side of reaction Formula is as follows:
CaO·MgO·SiO2→CaO+MgO+SiO2
6, sintered state mixture is being milled down to 140 mesh, and chromium oxide therein, nickel oxide, cobalt oxide, iron oxide etc. have magnetism, After ball mill discharging, it can be recycled by magnetic separation, the valuable metal oxide as high value by magnetic separator.Its Remaining mixture is the primary raw material of Si, Ca, Mg, K fertilizer.
Innovative point of the invention:
1. among serpentine, potassium chloride 6% is added, for reducing fusing point of the serpentine in calcination process, Si, Ca, Mg, K fertilizer is supplemented Potassium element.
2. addition reducing agent carbon and calcium carbonate, the chemical reaction of generation can make the oxidation among serpentine among serpentine Lead is able to enter among dedusting ash, is recycled.
3. the mixture ball milling of sintered state to 140 mesh, is the wear phases such as CrO, FeO, CdO, NiO, CoO and silicate, partially The best critical value that silicate, monticellite mutually dissociate.
Embodiment: embodiment is according to the serpentine resource and cement rotary kiln production line for gulping down Bu Lake with Ruoqiang county Example.
A method of Si, Ca, Mg, K fertilizer being produced using rotary kiln calcining serpentine, is included the following steps:
1, roping serpentine, lime stone (CaO > 50%), potassium chloride raw material to cement producing line;
2, prepare it is carbon containing be greater than 80% graphite it is stand-by to production line;
3, by above raw material according to the ratio of mass percent: serpentine: lime stone: potassium chloride: graphitic carbon=63%:28%: The ratio of 6%:3% is added to rotary kiln, calcines in 850~1200 DEG C of ranges, temperature of charge, which reaches 900 DEG C or more, to be gone out Material;
4, the material after discharging is milled down to 140 mesh in clinker grinding mill, by magnetic belt separator magnetic separation after discharging, magneticly elects magnetic Material is utilized as metallurgical raw material, does not have magnetic material to use as the powder raw material of Si, Ca, Mg, K fertilizer.
5, more than chemical examination powder raw material, detects CaO, SiO therein2、K2O, MgO and chromium therein, cadmium, arsenic, lead, The content of mercury.
6, after above detection, CaO insufficient section is supplied, K with desulfurized gypsum2O is insufficient, is supplied by potassium sulfate, Then in pelletizing production line, production becomes pelletized product.
7, the dedusting ash of rotary kiln is sold to Lead And Zinc Smelter as lead-zinc smelting raw material.

Claims (1)

1. a kind of method using rotary kiln calcining serpentine production Si, Ca, Mg, K fertilizer, characterized by the following steps: 1, Roping serpentine, lime stone, potassium chloride raw material to cement producing line, wherein the CaO mass percentage content in lime stone is at least It is 50%;2, prepare it is carbon containing be greater than 80% graphite it is stand-by to the production line;3, by above raw material according to mass percent Ratio: serpentine: lime stone: potassium chloride: graphitic carbon=63%:28%:6%:3% ratio is added to rotary kiln, 850~ 1200 DEG C of temperature range calcining, temperature of charge, which reaches 900 DEG C or more, to discharge;4, the material after discharging is levigate in clinker grinding mill To 140 mesh, by magnetic belt separator magnetic separation after discharging, magneticly elects magnetic material and utilized as metallurgical raw material, without magnetism Material used as the powder raw material of Si, Ca, Mg, K fertilizer;5, more than chemical examination powder raw material, detects CaO, SiO therein2、 K2O, the content of MgO and chromium therein, cadmium, arsenic, lead, mercury;6, after above detection, CaO insufficient section uses desulfurization Gypsum is supplied, K2O is insufficient, is supplied by potassium sulfate, and then in pelletizing production line, production becomes pelletized product;7, it rotates The dedusting ash of kiln is sold to Lead And Zinc Smelter as lead-zinc smelting raw material.
CN201811360575.9A 2018-11-15 2018-11-15 A method of Si, Ca, Mg, K fertilizer is produced using rotary kiln calcining serpentine Pending CN109180277A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1785917A (en) * 2005-12-08 2006-06-14 李书礼 Potassium magnesium fertilizer and its preparation method
CN1982260A (en) * 2005-12-12 2007-06-20 米清海 Slow-effect/release-controllable silica-potassic-magnesium fertilizer
CN103540768A (en) * 2013-10-18 2014-01-29 左晓娟 Integrated serpentine nickel element smelting process
KR20140055369A (en) * 2012-10-31 2014-05-09 김영욱 A plants nutrient solution process utilization of rice bran and mineral powder
CN106810320A (en) * 2017-01-17 2017-06-09 华南农业大学 Application and manufacture method of the activator in terms of cooling calcining manufacture activation potash fertilizer

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1785917A (en) * 2005-12-08 2006-06-14 李书礼 Potassium magnesium fertilizer and its preparation method
CN1982260A (en) * 2005-12-12 2007-06-20 米清海 Slow-effect/release-controllable silica-potassic-magnesium fertilizer
KR20140055369A (en) * 2012-10-31 2014-05-09 김영욱 A plants nutrient solution process utilization of rice bran and mineral powder
CN103540768A (en) * 2013-10-18 2014-01-29 左晓娟 Integrated serpentine nickel element smelting process
CN106810320A (en) * 2017-01-17 2017-06-09 华南农业大学 Application and manufacture method of the activator in terms of cooling calcining manufacture activation potash fertilizer

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
郭俊才: "《水泥及混凝土技术进展》", 30 June 1993, 中国建材工业出版社 *

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Application publication date: 20190111