CN1054759A - With green bean rock system potash fertilizer and comprehensive utilization process thereof - Google Patents
With green bean rock system potash fertilizer and comprehensive utilization process thereof Download PDFInfo
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- CN1054759A CN1054759A CN 91107119 CN91107119A CN1054759A CN 1054759 A CN1054759 A CN 1054759A CN 91107119 CN91107119 CN 91107119 CN 91107119 A CN91107119 A CN 91107119A CN 1054759 A CN1054759 A CN 1054759A
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- potassium
- green bean
- active silica
- bean rock
- fertilizer
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- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
Relate to a kind of low temperature acid water of decomposition micacization green bean rock with green bean rock system potash fertilizer and comprehensive utilization process thereof and produce agricultural water-soluble potassium nitrogenous fertilizer, active silica, aluminium hydroxide, 4 zeolite products and technical process and technical requirements.K in the green bean rock
2The O extraction yield is greater than 85%, and the potassium-nitrogen fertilizer of producing contains K2O15-17%, N13-15%; Active silica whiteness 80-85%, specific surface 120-130m2/g, pore volume 0.4-0.5cm3/g; 4 molecular sieves can be used for washing auxiliary detergent, its whiteness 88-91%, and the calcium ion-exchanged amount is greater than 290mgCaCO3/g (exchange process).
Description
Prior art: produce potash fertilizer with potassium bearing rock, all need high temperature sintering or fusion.Its method has shaft kiln legal system potash-lime fertilizer, blast furnace legal system silicon-magnesium potash fertilizer and fused(calcium magnesium phosphorus)potash fertilizer etc.Public technology:
1.1989 year June, " inorganic chemical technology is learned (three) chemical fertilizer " the 70th page " with potassium felspar sand system salt of wormwood and white fused cement " that chemical industry press publishes, be that various raw materials such as potassium felspar sand, Wingdale, rhombspar, bauxitic clay, fluorite and coal are crushed to certain particle size respectively, through screening, batching, send into blast furnace, at high temperature react, when temperature up to 1000 ℃~1300 ℃ the time, K
2O is displaced to begin to volatilize and overflows with furnace gas, meet carbonic acid gas and promptly generate salt of wormwood, the various coloring metal oxide compounds that contain in the furnace charge are reduced into metal by carbon and carbon monoxide, thereby separate with slag, this slag decolouring is white, can be used as the grog of white fused cement.
2. in October, 1978, the second geology group of former National Geology general bureau is at " Sichuan Province's potassium rich rock distribution overview, system potash fertilizer technology and farmland manure trial consolidated report " in the 71st page-98 pages a kind of silicon-magnesium potash fertilizer technology of producing is provided: with potassium rich rock (green bean rock), rhombspar, coal, pulverize and cooperation by a certain percentage, add in the blast furnace, allow furnace charge at high temperature react, when temperature during up to 1450~1500 ℃, melt becomes the melt of good fluidity, it is come out from blast furnace discharge port jet flow, under shrend, sharply cool off, become the black glass matter fertilizer of amorphism, drying, ball milling silicon-magnesium potash fertilizer.
The method that the objective of the invention is to avoid above-mentioned deficiency of the prior art and propose the sour low-temperature decomposition green bean rock of a kind of usefulness, its method technical process is simple, easy to use, free from environmental pollution, produce potassium-nitrogen fertilizer, aluminium hydroxide, active silica, 4 applicable to different scales
Products such as molecular sieve.
Solution of the present invention is: use the green bean rock of damouritization, with its pulverizing, add water and smash slurry, remove impurity, adding sulfuric acid furnishing liquid-solid ratio is 2: 1, and acidity is the slip of 30-40%, stirs, is heated to 100-120 ℃ in acid-resistant reactor, reacted 4-8 hour, filter fast while hot, clean insoluble slag with hot water, this slag is the active silica product of being produced.With filtrate evaporation concentration, cooling, stir, separate out potassium alum, again potassium alum is placed that ammonia soaks in the ammonia immersion trough, heated and stirred after ammonia soaks and reacts completely, is filtered simultaneously, cleans insoluble slag, oven dry promptly gets the aluminium hydroxide product of being produced; Filtrate evaporation concentration, crystallization make the potassium-nitrogen fertilizer product.
The present invention is the byproduct of used water micacization green bean rock system potassium-nitrogen fertilizer also: active silica and aluminium hydroxide produce 4
Molecular sieve, its solution are with active silica and aluminium hydroxide, press SiO
2: Al
2O
3=2: 1 ratio, in the caustic soda soln of 5-10%, water heat agitated crystallization method synthetic 4
Molecular sieve washing auxiliary detergent product.
Advantage of the present invention is:
1. adopt low temperature to decompose the green bean rock ore, need not put up a kiln and blast furnace, do not need ore high temperature sintering or fusion with acid.
2. the present invention produces multiple product, no mine tailing, pollution-free, comprehensive utilization degree height with a kind of rock.
3. the active silica of producing with the present invention is different from other silica gel products, about pore volume is twice than general silica gel product.
4. produce K in the green bean rock by technical process of the present invention and technical requirements
2The O extraction yield is greater than 85%, and rock per ton can be produced:
(1) soluble potassium nitrogenous fertilizer [(K, NH
4)
2SO
4] 360~400Kg, contain K
2O15~17%, N13-15%.
(2) active silica 400~450Kg, whiteness 80-85%, specific surface 120-130m
2/ g, pore volume 0.4~0.5cm
3/ g.
(3) 4
Molecular sieve 400-500Kg, whiteness 88-91%, the calcium ion-exchanged amount is greater than 290mgCaCO
3Exchange process of/g().
5. the product of producing with the present invention can further be produced efficient catalytic agent carrier, high-performance solid acetylene gas scavenging agent, white carbon black, light magnesium oxide and be used for the energy-conservation starting material etc. of synthetic microporous Calucium Silicate powder.
6. the present invention need not add any other auxiliary material when decomposing green bean rock.
7. technical process is simple, easy to operate, is applicable to the production of different scales.
Product of the present invention and technical process and technical requirements are provided by the following drawings and embodiment:
Fig. 1 is with green bean rock system active silica, aluminium hydroxide and potassium-nitrogen fertilizer technical process schematic block diagram
The present invention produces potassium-nitrogen fertilizer, aluminium hydroxide, active silica and 4 in conjunction with Fig. 1, Fig. 2 to being distributed in the west and south, Sichuan damouritization green bean rock
The embodiment of zeolite product elaborates.
Fig. 1, with the green bean rock ore pulverizing (1) of damouritization, add suitable quantity of water and smash slurry (2) 30-60 minute, after leaving standstill 3-10 minute, get upper strata slurries (abandoning the coarse grain and the impurity that sink to the bottom), with sulfuric acid furnishing solid-to-liquid ratio is 1: 2, acidity is 30~40% slip (3), in acid-resistant reactor, stir, thermal degradation (4), react 4-8 hour (under the high-temperature pressurizing condition in 100-120 ℃ under the normal pressure, reaction times shortens dramatically), filter fast while hot then (5), clean insoluble slag with hot water, this slag is active silica (6), amalgamation liquid (7) (being filtrate and part washings) is when being evaporated to 1.3~1.5 times of volumes of former liquid phase in vaporizer, cooling rapidly, and stir fully continuously, till having a large amount of potassium alum crystallizations (8) to separate out, filter (9) and isolate potassium alum crystallization (10), and with the separating agent of this potassium alum as potassium element, and then produce soluble potassium nitrogenous fertilizer and aluminium hydroxide, after filtrate (11) is replenished a certain amount of sulfuric acid, return (2), this process circulation secondary after separating out potassium alum (10), concentrates filtrate (11) continuation for the third time, fractional crystallization is separated out Al respectively
2(SO
4)
318H
2O, MgSO
47H
2The O(coarse products), again will be for the third time mother liquor behind the crystallization be used to make the solvent of other Chemicals.
Potassium alum places ammonia immersion trough (12) to carry out ammonia to soak, heated and stirred (13), after treating that aluminum hydroxide precipitation fully, with sedimentation and filtration, clean (14), dry aluminium hydroxide (15) product that gets, filtrate (16) is filtered (18) and can be got product potassium-nitrogen fertilizer (19) through evaporation, crystallization (17), and mother liquor (20) returns the production [also filtrate (16) direct evaporation can be got potassium-nitrogen fertilizer (19)] that (12) continue on for potassium-nitrogen fertilizer.
Fig. 2, active silica (21) and aluminium hydroxide (22) are pressed SiO
2: Al
2O
3=2: 1 ratio, in the caustic soda soln of 5-10% (23), water heat agitated crystallization (24) method synthetic 4
Molecular sieve after filtration, clean (25), will precipitate that (26) dry (27), levigate (28) promptly get 4
Zeolite product (29) can be made washing auxiliary detergent and use, and filtrate (30) is returned (23) and continued to use.
Claims (3)
1, a kind of processing method of producing agricultural potash fertilizer with potassium bearing rock, it is characterized in that will be the damouritization green bean rock do not add batching and directly pulverize, add water and smash the slurry removal of impurity, add sour furnishing solid-to-liquid ratio and be 1: 2, acidity is the slip of 30-40%, in acid-resistant reactor, stir, be heated to 100-120 ℃, reacted 4-8 hour, filtered while hot is cleaned insoluble slag with hot water, and this slag is the active silica product of being produced.Filtrate is stirred evaporation concentration, cooling, separate and separate out potassium alum, aluminum hydroxide precipitation is come out, filter and promptly get the aluminium hydroxide product with ammonia leaching process.Filtrate evaporation concentration, crystallization promptly get the potassium-nitrogen fertilizer product.
2, aluminum hydroxide precipitation is come out with ammonia leaching process according to the described potassium alum of claim 1, it is characterized in that placing the interior ammonia of ammonia immersion trough (jar) to soak potassium alum, heated and stirred impels aluminum hydroxide precipitation complete.
3, a kind of byproduct active silica and aluminium hydroxide with damouritization green bean rock system potassium-nitrogen fertilizer produces 4
The method of molecular sieve is characterized in that active silica and aluminium hydroxide are pressed SiO
2: Al
2O
3=2: 1 ratio, in the caustic soda soln of 5-10%, water heat agitated crystallization method is synthetic.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 91107119 CN1054759A (en) | 1989-10-19 | 1991-01-14 | With green bean rock system potash fertilizer and comprehensive utilization process thereof |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA 2001062 CA2001062A1 (en) | 1989-10-19 | 1989-10-19 | Method of heat-treating unstable ceramics by microwave heating and susceptors used therefor |
CN 91107119 CN1054759A (en) | 1989-10-19 | 1991-01-14 | With green bean rock system potash fertilizer and comprehensive utilization process thereof |
Publications (1)
Publication Number | Publication Date |
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CN1054759A true CN1054759A (en) | 1991-09-25 |
Family
ID=25673772
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CN 91107119 Pending CN1054759A (en) | 1989-10-19 | 1991-01-14 | With green bean rock system potash fertilizer and comprehensive utilization process thereof |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102775219A (en) * | 2012-08-21 | 2012-11-14 | 中国科学院青海盐湖研究所 | Method for preparing nitrogen-phosphorus-potassium compound fertilizer from biotite |
CN102838138A (en) * | 2012-09-11 | 2012-12-26 | 昊青薪材(北京)技术有限公司 | Process for preparing agricultural ammonium potassium sulfate from biotite powder |
CN111439754A (en) * | 2020-05-22 | 2020-07-24 | 四川君和环保股份有限公司 | Comprehensive utilization method of mung bean rock |
CN111498858A (en) * | 2020-05-22 | 2020-08-07 | 四川君和环保股份有限公司 | Mung bean rock utilization method |
-
1991
- 1991-01-14 CN CN 91107119 patent/CN1054759A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102775219A (en) * | 2012-08-21 | 2012-11-14 | 中国科学院青海盐湖研究所 | Method for preparing nitrogen-phosphorus-potassium compound fertilizer from biotite |
CN102838138A (en) * | 2012-09-11 | 2012-12-26 | 昊青薪材(北京)技术有限公司 | Process for preparing agricultural ammonium potassium sulfate from biotite powder |
CN111439754A (en) * | 2020-05-22 | 2020-07-24 | 四川君和环保股份有限公司 | Comprehensive utilization method of mung bean rock |
CN111498858A (en) * | 2020-05-22 | 2020-08-07 | 四川君和环保股份有限公司 | Mung bean rock utilization method |
CN111439754B (en) * | 2020-05-22 | 2021-01-15 | 四川君和环保股份有限公司 | Comprehensive utilization method of mung bean rock |
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