CN101885514B - Preparation for ultrafine anhydrous sulfate by a two-step method - Google Patents

Preparation for ultrafine anhydrous sulfate by a two-step method Download PDF

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Publication number
CN101885514B
CN101885514B CN2010102144748A CN201010214474A CN101885514B CN 101885514 B CN101885514 B CN 101885514B CN 2010102144748 A CN2010102144748 A CN 2010102144748A CN 201010214474 A CN201010214474 A CN 201010214474A CN 101885514 B CN101885514 B CN 101885514B
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sulfate
dehydration
time
crushing
ultrafine anhydrous
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CN101885514A (en
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吕文广
郑景宜
吕铂颐
郑玉琦
唱祺
陈译哲
孙健
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Zheng Jingyi
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JILIN CITY FRIEND TECHNOLOGY Co Ltd
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Abstract

The invention discloses preparation of ultrafine anhydrous sulfate by a two-step method. The sulfate is prepared by the following steps: calcinating and crushing sulfate crystal containing crystal water after the crystal is subjected to expansion drying and crushing at the temperature of 100-150 DEG C, and performing primary dehydration and crushing by using a drying and crushing combined machine invented by the inventor (China patent application number is 200920093766.3); and performing secondary drying and crushing by using a rotary kiln for uniform calcination of inorganic salt invented by the inventor (China patent application number is 200820072472.8). The preparation has better effect and higher efficiency, solves the problems that the sulfate crystal is easily hardened and caked, is difficult to crush and has long manufacture time, large granularity, hard control and high cost in the dehydration process of directly sintering the sulfate crystal; and the prepared ultrafine anhydrous sulfate has controllable granularity of between 2 and 10mu m on average, good dispersion, short production process, high yield and low cost; and when being used as feed or other additives, the ultrafine anhydrous sulfate should be mixed uniformly.

Description

Two-step approach prepares ultrafine anhydrous sulfate
Technical field
The invention belongs to chemical field, is raw material with the vitriol that contains crystal water specifically, prepares ultrafine anhydrous sulfate with two-step approach.
Sweden chemist Brandt has restored cobalt metal in 1735 from cobalt ore (CoAsS), Azary in 1879 points out cobalt, and hematopoiesis has superperformance to body.Filmer reported first in 1933 scarce cobalt animal can produce serious anaemia, nineteen thirty-five cobalt be trace element essential in people and the Animal nutrition certainly formally.
Cobalt is positioned at d district VIII family in the periodic table of elements, close the title iron group with iron, nickel, is the necessary trace element of human body, with the form performance physiological action of cobalamin, participates in synthetic and the fat and the carbohydrate metabolism of nucleic acid, choline, methionine(Met).When prevention and treatment endemic goiter, that cobalt and iodine associating result of use is better.Cobalt can also improve the biological activity of zinc, makes zinc be easy to absorb.Cobalt can be kept the homergy of nucleic acid, when it lacks, can disturb duplicating of DNA, makes it to produce error, causes some functional deterioration, the metabolic disturbance of cell even causes necrocytosis.Scarce cobalt can cause cardiovascular diseases, anaemia, myelitis and glaucoma etc.Cobalt is the micro-metals with special biological function that microorganism growth needs, and exists close interaction between itself and the mikrobe.Cobalt is participated in the composition of cobalamin and the symbiotic nitrogen fixation of mikrobe and plant.
Cobalt can promote the utilization of non-protein nitrogen(NPN), if diet lacks cobalt, synthesizing slowly of cobalamin influences the utilization of nitrogenous substances in the diet.Cobalt can promote to feed ox with non-pulse family hay to the utilization of urea with to cellulosic digestion, and can improve the speed of growth of ox.When the ruminating animal that grows up when feeding lacked the cobalt daily ration, the cobalamin of storing in the liver was enough kept several weeks.And the reserves of cobalamin are lower in children's ruminating animal liver in age, so they lack very sensitivity to cobalt.The early symptom that cobalt lacks is growth retardation, become thin, weightlessness.More serious symptom is a fat acid decomposition in the liver, the extreme anaemia, and anti-infection ability descends, and the neutrophilic granulocyte function is impaired.
Pig has adds the report that cobalt promotes growth and improves efficiency of feed utilization, also can utilize the report of cobalt composite part cobalamin relevant for the terminal mikrobe of swine alimentary canal.In feed, often allocate the cobalt of 0.1mg/kg into, the sure needs that satisfy pig.When ruminating animal diet cobalt is lower than 0.08mg/kg, poor appetite, poor growth, anaemia is like muscular dystrophy etc.Cobalt disease can appear lacking.When replenishing cobalt to ruminating animal, the injection cobalt has little effect; Must oral administration give.
Though cobalt is the low toxicity element to animal, contains cobalt 400mg/kg in the swine rations children piglet in age is poisoned; Milk cow and beef cattle maximum safety are per kilogram daily ration 10 1 20mg, and sheep then is 50mg, and chicken is responsive, is 4mg.Animal feedstuff contains abundant cobalt, the about 0.8-1.6mg/kg of content, and it is 0.1-0.25mg/kg that normal herbage contains the cobalt amount, and it is low that cereal seed feed contains the cobalt amount, and per kilogram is 0.06-0.09mg only.
Along with science and technology development; Livestock industry intensive culture scale is increasing; In order to reduce cost to greatest extent, forage compounding requires more and more stricter, the cobalt additive that in mixed feed, uses have rose vitriol (, powder blue, cobaltous carbonate, NSC 51149 and Cobaltous diacetate etc.But because its processing characteristics and price is different, use contains the rose vitriol of crystal water, the heptahydrate of widespread usage mostly.
Cobalt is a trace mineral supplement in daily ration, and addition is about 0.1mg/kg, because conventional rose vitriol is aqueous xln, particle size differs, and caking is difficult to mix easily, and the intake of animal individual has more lacks weak effect.
Anhydrous cobaltous sulfate is the mazarine cubic system, specific density 3.71 (25 ℃), and 735 ℃ of fusing points do not lump.Can make by 7 water rose vitriol calcination; If but direct calcination heptahydrate, the crystal dehydration is prone to caking, forms very hard block, is difficult to pulverize, and the time is long, granularity is big and be not easy control, and technology is loaded down with trivial details, the cost height.
Also there is same problem when producing anhydrous sulfate with other vitriol that contains crystal water.For example: single nickel salt (7 water or 6 water), copper sulfate (5 water), zinc sulfate (7 water), sal epsom (7 water) and zirconium sulfate (4 water).
Summary of the invention
The purpose of this invention is to provide two-step approach and prepare ultrafine anhydrous sulfate, it comprises:
Dehydration for the first time: the sulphate crystal body that will contain crystal water under temperature 100-150 ℃, expansion drying, pulverizing;
Dehydration for the second time: after expansion drying, the powder essence, roasting again, pulverizing;
Dehydration temperaturre for the second time: rose vitriol is 400-450 ℃;
Zinc sulfate, zirconium sulfate, single nickel salt temperature are 300-350 ℃;
Sal epsom is 200-250 ℃;
The dehydration temperaturre first time of copper sulfate is 100 ℃, and dehydration temperaturre is 160-200 ℃ for the second time;
The described dehydration first time, use Chinese patent drying and crushing all-in-one, application number: 200920093766.3, expansion drying, pulverizing;
The described dehydration second time, use a kind of inorganic salt uniform calcination rotary kiln of Chinese patent, application number: 200820072472.8, carry out roasting;
The described rose vitriol that contains crystal water is a heptahydrate;
Rose vitriol first dehydration temperaturre is 130-140 ℃.
Two-step approach of the present invention prepares ultrafine anhydrous sulfate; The vitriol that will contain crystal water is under temperature 100-150 ℃, after expansion drying, the pulverizing; Roast is pulverized again; Carry out twice dehydration and pulverize, dehydration is for the first time pulverized, and uses the drying and crushing all-in-one that the inventor develops voluntarily (one Chinese patent application number: 200920093766.3); Dehydration is for the second time pulverized, and (one Chinese patent application number: 200820072472.8), effect is better, efficient is higher to use a kind of inorganic salt uniform calcination rotary kiln that the inventor designs voluntarily.Solve the vitriol dehydration that direct calcination contains crystal water and be prone to caking, has formed very hard block, be difficult to pulverizing, and the problem that long processing time, granularity are not easy greatly to control, cost is high.The ultrafine anhydrous sulfate that makes, globule size is controlled, and mean particle size can reach 2-10 μ m, and good dispersivity during as feed or the use of other additive, mixes, and production process is short, and output is high, and cost is low.
Embodiment
Embodiment 1 two-step approach prepares super-fine anhydrous rose vitriol
Dehydration for the first time: the rose vitriol xln that will contain 1 crystal water under 100 ℃ of temperature, expansion drying, pulverizing;
Dehydration for the second time: after expansion drying, the pulverizing, under 450 ℃ of temperature, roasting is ground.
Embodiment 2 two-step approachs prepare super-fine anhydrous rose vitriol
Dehydration for the first time: the rose vitriol xln that will contain 7 crystal water under 150 ℃ of temperature, expansion drying, pulverizing;
Dehydration for the second time: after expansion drying, the pulverizing, under 400 ℃ of temperature, roasting is ground.
Embodiment 3 two-step approachs prepare super-fine anhydrous rose vitriol
Dehydration for the first time, the rose vitriol xln that will contain 7 crystal water under 140 ℃ of temperature, expansion drying, pulverizing;
Dehydration for the second time, after the oven dry powder essence, under 420 ℃ of temperature, roasting is ground.
Embodiment 4 two-step approachs prepare super-fine anhydrous rose vitriol
Dehydration for the first time: with Chinese patent, (application number: 200920093766.3), temperature transfers to 130-140 ℃ to the drying and crushing all-in-one, and feeder adds the rose vitriol xln that contains crystal water and pulverizes, dries;
Dehydration for the second time: with Chinese patent, (application number: 200820072472.8), temperature transfers to 400-450 ℃ to a kind of inorganic salt uniform calcination rotary kiln, pours the rose vitriol after pulverizing, drying into feeding mechanism, carries out roasting, and the rod milling system grinds.
The super-fine anhydrous rose vitriol that embodiment 1-4 makes, globule size is controlled, and uniform particles, mean particle size can reach 2-10 μ m, and cobalt contents is about 30%; Good dispersivity, cobalt contents are stablized.
Embodiment 5
Two-step approach prepares super-fine anhydrous single nickel salt, copper sulfate, zinc sulfate, sal epsom or zirconium sulfate, and for the first time dehydration temperaturre is specifically seen table 1 with dehydration temperaturre for the second time, and other repeats embodiment 4.
The super-fine anhydrous single nickel salt, copper sulfate, zinc sulfate, sal epsom or the zirconium sulfate that make, globule size is controlled, and uniform particles, mean particle size can reach 2-10 μ m, good dispersivity.
Table 1
The inorganic salt title Dehydration temperaturre expansion drying, pulverizing for the first time Dry, the pulverizing of dehydration temperaturre roasting for the second time
Single nickel salt (7 water or 6 water) 100-150 300-350
Copper sulfate (5 water) 100 160-200
Zinc sulfate (7 water) 100-150 300-350
Sal epsom (7 water) 100-150 200-250
Zirconium sulfate (4 water) 100-150 300-350

Claims (6)

1. two-step approach prepares the method for ultrafine anhydrous sulfate, and it comprises:
Dehydration for the first time: the sulphate crystal body that will contain crystal water under temperature 100-150 ℃, expansion drying, pulverizing;
Dehydration for the second time: after expansion drying, the powder essence, roasting again, pulverizing;
Get the anhydrous sulfate of granularity 2-10 μ m;
Described vitriol is rose vitriol, single nickel salt, copper sulfate, zinc sulfate, sal epsom or zirconium sulfate.
2. two-step approach according to claim 1 prepares the method for ultrafine anhydrous sulfate, it is characterized in that: dehydration temperaturre for the second time: rose vitriol is 400-450 ℃, and zinc sulfate, zirconium sulfate, single nickel salt are 300-350 ℃, and sal epsom is 200-250 ℃; The dehydration temperaturre first time of copper sulfate is 100 ℃, and dehydration temperaturre is 160-200 ℃ for the second time.
3. two-step approach according to claim 1 and 2 prepares the method for ultrafine anhydrous sulfate, it is characterized in that: dehydration for the first time, use Chinese patent drying and crushing all-in-one, application number: and 200920093766.3, expansion drying, pulverizing.
4. two-step approach according to claim 3 prepares the method for ultrafine anhydrous sulfate, it is characterized in that: dehydration for the second time, use a kind of inorganic salt uniform calcination rotary kiln of Chinese patent, application number: and 200820072472.8, carry out roasting.
5. two-step approach according to claim 4 prepares the method for ultrafine anhydrous sulfate, it is characterized in that: the rose vitriol that contains crystal water is a heptahydrate.
6. two-step approach according to claim 5 prepares the method for ultrafine anhydrous sulfate, it is characterized in that: the dehydration temperaturre first time of heptahydrate is 130-140 ℃.
CN2010102144748A 2010-07-01 2010-07-01 Preparation for ultrafine anhydrous sulfate by a two-step method Expired - Fee Related CN101885514B (en)

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3377273A (en) * 1965-02-17 1968-04-09 Atomic Energy Authority Uk Process and apparatus for desalination of an aqueous solution containing calcium sulphate
CN1327949A (en) * 2000-06-08 2001-12-26 徐万清 Cool-hot fusion method for preparing anhydrous sodium sulfate and its hot-fusion tower
CN1544331A (en) * 2003-11-14 2004-11-10 天津市昌昊化工股份合作公司 Magnesium sulfate production method using magnesium oxide and desulfurated waste fluid
CN1810728A (en) * 2005-11-02 2006-08-02 大连爱思凯矿产有限公司 Natural granular magnesium sulfate fertilizer and its prepn process
CN201289292Y (en) * 2008-09-19 2009-08-12 吉林市弗兰达科技股份有限公司 Rotary kiln for uniform calcination of inorganic salt
CN201413016Y (en) * 2009-06-09 2010-02-24 吕文广 Drying and crushing combined machine

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3377273A (en) * 1965-02-17 1968-04-09 Atomic Energy Authority Uk Process and apparatus for desalination of an aqueous solution containing calcium sulphate
CN1327949A (en) * 2000-06-08 2001-12-26 徐万清 Cool-hot fusion method for preparing anhydrous sodium sulfate and its hot-fusion tower
CN1544331A (en) * 2003-11-14 2004-11-10 天津市昌昊化工股份合作公司 Magnesium sulfate production method using magnesium oxide and desulfurated waste fluid
CN1810728A (en) * 2005-11-02 2006-08-02 大连爱思凯矿产有限公司 Natural granular magnesium sulfate fertilizer and its prepn process
CN201289292Y (en) * 2008-09-19 2009-08-12 吉林市弗兰达科技股份有限公司 Rotary kiln for uniform calcination of inorganic salt
CN201413016Y (en) * 2009-06-09 2010-02-24 吕文广 Drying and crushing combined machine

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
栾昊.旋转闪蒸干燥技术在盐化工生产中的应用.《中国井矿盐》.2003,第34卷(第06期),32-35. *

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