CN204079502U - KCl production system produced by a kind of novel carnallitite - Google Patents
KCl production system produced by a kind of novel carnallitite Download PDFInfo
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- CN204079502U CN204079502U CN201420382428.2U CN201420382428U CN204079502U CN 204079502 U CN204079502 U CN 204079502U CN 201420382428 U CN201420382428 U CN 201420382428U CN 204079502 U CN204079502 U CN 204079502U
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Abstract
The utility model discloses a kind of novel producing potassium chloride from carnallite production system, comprise and add ore deposit equipment, crystallizer, floatation equipment, filter plant, again plasm scouring equipment, centrifugal-dehydration device, dry packing equipment, each equipment is linked in sequence; Increase crusher in described adding on the equipment of ore deposit, be convenient to crystal system decomposition and crystallization; Simultaneously in crystallizer, a kind of novel crystallization device of our company's invention is used to replace original cool technology---the carnallitite resolving device of direct floatation process.The utility model improves the manufacturing condition of former direct floatation process, and the Repone K rate of recovery brings up to 60%, and eliminating purity is 90% Potassium Chloride Product, and Potassium Chloride Product purity is brought up to 93% ~ 95%, and product granularity increases, and energy consumption reduces.
Description
Technical field
The utility model belongs to gas chemical industry and salt chemical engineering field, and particularly a kind of salt-pan carnallite ore deposit is that raw material adopts direct flotation method to produce the production system of Repone K.
Background technology
China is a large agricultural country, and the development of agricultural be unable to do without chemical fertilizer.China's agricultural fertilizer also exists nitrogen for a long time, phosphorus, potassium are out of proportion, and soil potassium deficiency becomes one of important factor affecting China's agricultural development.
Along with the raising of China's potassium resource development technique, especially Qinghai Salt Lake Industry Co., Ltd. is to the raising of the exploitation of Cha Er Han Salt Lake resource and enterprise self science and technology, potassium resource exploitation in salt lake is formed to the situation of kinds of processes associating, current China Repone K complete processing mainly contains: cool technology-direct flotation method technique, crystallization method technique, reverse flotation-cold crystallization technique, convert the Joint Implementation of the kinds of processes such as halogen technique.
Cool technology---direct floatation process is external conventional machining process realization at home the earliest, and its technical process is material loading → decomposition → flotation → filtration → washing, dehydration → dry, packaging.Accompanying drawing 1 is shown in technical process.
As traditional potash fertilizer production technique, this explained hereafter device accounts for more than 80% of China's Caidamu Basin KCl production overall apparatus.The Potassium Chloride Product KCE content that initial cool technology---direct floatation process device is produced only has 70% ~ 80%, moisture content is 8% ~ 10%, by updating, product KCE content reaches about 90%, moisture content is 6%, quality product reaches the agriculture acceptable end product of GB6549-1996, reaches the technological standard of the agriculture salable product of revised GB6549-2011.As traditional potassium chloride production process, cool technology---direct floatation process has following advantage: (1) process, due to this technique exploitation and research comparatively early, constantly perfect through for many years, technical process has been tending towards ripe.With regard to flotation itself, amine collector is functional as the collecting agent of Repone K, and sorting result is obvious.(2) technical process is simple.(3) raw ore strong adaptability, in utilization, in low grade potassium ore deposit, advantage is given prominence to.But this technique, compared with the reverse flotation-cold crystallization technique of Qinghai Salt Lake Industry Co., Ltd.'s independent research, also has the defect of self, is mainly manifested in: (1) Repone K system recoveries rate is lower, and quality product not easily improves.This technological operation control overflow is strict, has impact, be lost in mother liquor as carnallitite decomposes the excessive Repone K of in raw material about 50% that causes that adds water to ore control, decomposition water rate control, floating operation, flotation reagent etc. on the rate of recovery and quality product; Floatation process Repone K and sodium-chlor inferior separating effect, in concentrate foam, sodium-chlor is carried secretly more, and in discarded tail salt, KCE content is high, and what have is even greater than 8%, utilizes standard close to industrial raw ore; Quality product is difficult to the industrial potassium chloride premium grads index that is up to state standards.(2) product granularity is thin, not easily dry, thus cause product water loss and Sweet natural gas energy consumption high, tail liquid emissions amount is high.
Summary of the invention
Goal of the invention: by cold crystallization technology transplant in direct floatation process,---reverse floatation process and cool technology---the learning from other's strong points to offset one's weaknesses of direct floatation process that realize cold crystallization, the advantages realizing two techniques, overcomes cool technology---direct floatation process produce exist in Repone K process defect, improve system recoveries rate, improve the quality of products, reduce production energy consumption.
Technical scheme: the purpose of this utility model is realized by following technical proposals:
A kind of novel producing potassium chloride from carnallite production system, comprise and add ore deposit equipment, crystallizer, floatation equipment, filter plant, again plasm scouring equipment, centrifugal-dehydration device, dry packing equipment, each equipment is linked in sequence;
Ore deposit equipment increases crusher on original, make larger carnallitite be able to fragmentation and diminish, be convenient to crystal system decomposition and crystallization;
Simultaneously in crystallizer, a kind of novel crystallization device (patent of invention number: ZL201310040807.3) of our company's invention is used to replace original cool technology---the carnallitite resolving device of direct floatation process, cool technology---in direct floatation process, cool technology system is by carnallitite hydrolyzable, due to key equipment---decompose the simple structure of tank, the residence time of carnallitite in decomposition tank is short, therefore Repone K does not have enough time to realize the increase of particle, and required decomposition amount of water is larger.The key equipment of cold crystallization system in the present invention---its tectonic division of novel crystallization device is negative area, dissolve area, region, three, race way, dissolve area is added above race way, extend the residence time of low-sodium carnalite in this region, make mixing evenly, reaction is more abundant, carnallitite reaches and decomposes completely; Owing to adding sedimentation crystallizing field volume, the Repone K after decomposition has time enough to grow up in crystallizing field.The ring-type mother liquor distributor that novel crystallization device is arranged around inner core pyramidal structure lower port, increase the contact area of mother liquor and low-sodium carnalite, be issued to the effect of abundant mixed decomposition at the stirring action of ejection liquid simultaneously, solve crystallizer in the past fully mixed decomposition just by the overflow of inner core top to the problem of crystalliser feet.Novel crystallization device height reduction, shortens stir shaft, improves stirrer operation stability, deduct stir shaft plummer-block simultaneously, reduce the fault point simultaneously, increases crystallizer continuous operating time, plays essence ensure the single tank production capacity of raising.CFD and FEA technology is have employed in tank body and stirrer design, field of flow and tank structure are optimized, decomposition reaction district scope is adjusted, increase the decomposition reaction district residence time, be beneficial to decomposition reaction fully to carry out, meet carnallitite decomposition and crystallization demand.Add sedimentation crystallizing field volume, actually increase output, reduce unit output energy consumption.
The production method of this novel producing potassium chloride from carnallite production system, concrete technology is as follows:
Add ore deposit: the carnallitite that system is shone in salt pan is transported in crude ore bin by gathering, adjust upper ore deposit amount through spiral and be transported to reciprocating sieve, crusher is entered after nugget larger in raw ore and other foreign material sieves being removed, crusher by crushing raw ore to below 20mm, be convenient to decomposition and the crystallization effect of crystallizer, carnallite after fragmentation is transported to crystallizer, carries out decomposition and crystallization;
Crystallization: the smart potassium mother liquor that the carnallite after described fragmentation and centrifugation systems produce, decompose fresh water and enter crystallizer, because of KCl, NaCl, MgCl simultaneously
2different solubility, MgCl
2first dissolve completely and be present in crystallizer with liquid form, KCl continues to dissolve formation KCl saturated solution, and along with the continuous increase adding ore deposit amount, KCL forms supersaturated solution crystallization.NaCl can not separate out liquid phase is unsaturated, and tiny NaCl dissolves and major part exists with solid phase particles form.Therefore complete the decomposition of carnallitite in crystallizer, increase Repone K grain size number simultaneously;
Flotation: the slurry pipeline transport after decomposition and crystallization is to the medicament mediation groove of floatation system, the flotation reagent added with floatation system metering chemical feeding device carries out being in harmonious proportion rear gravity flow and enters flotation machine, flotation operation adopts one roughing, recleaning, once purging selection, obtains thick potassium slip through flotation.Wherein selected froth product is from flowing to filtering system, and the filtrate after filtration is high mother liquid of magnesium, and carry out circulation and be used for regulating selected operation concentration, all the other deliver to tail salt pond by mine tailing;
Filter, plasm scouring, centrifuge dehydration again: after the horizontal stripes machine of the described thick potassium slip from floatation system system after filtration removes high mother liquid of magnesium, add fresh water in the wash agitation groove of plasm scouring system again, the magnesium chloride of removing absorption and sodium-chlor wherein.Slip whizzer after washing removes washing mother liquor (smart potassium mother liquor), becomes smart potassium, is delivered to dehumidification system drying.Essence potassium mother liquor reclaims with being pumped to crystallizer and replacing a part of fresh water to decompose carnallite after flowing to smart potassium mother liquor tank;
Dry, packaging: described from the smart potassium after centrifuge dewatering by Belt Conveying to whizzer, the hot blast by burning in drying machine carries out drying.Dried product is packed to wrapping machine by belt haulage.
Accompanying drawing 3 is shown in above technical process.
Direct floatation process compares cold crystallization---direct floatation process and cool technology---, carnallitite through broken with smart potassium mother liquor, decompose fresh water and enter crystallizer diversion district simultaneously, when controlling ore deposit amount, amount of water, underflow flow, stirring frequency well, be beneficial to and improve manufacturing condition, increase product K Cl granularity; Capacity of decomposition can be made effectively to be increased, improve and decompose Repone K yield; Along with the increase of KCl granularity, flotation three phase boundary is more stable, and sorting result is obvious, while raising flotation operation index, improves potassium yield.The increase of KCl granularity, be beneficial to horizontal stripes machine and centrifuge dewatering, water capacity reduces relatively, alleviates the difficulty of washing, and drying cost can be made to reduce, and product index is easy to control.
Advantage of the present utility model and beneficial effect: the utility model is to cool technology traditional at present---direct floatation process has mainly carried out two core transformations, add crusher, change former cool technology system into cold crystallization system, and adjustment is optimized to subsequent technique controling parameters, define a kind of novel potassium chloride production process; Maximum advantage instead of original cool technology system by cold crystallization system, by cold crystallization technology transplant to cool technology---in direct floatation process,---reverse floatation process and cool technology---the learning from other's strong points to offset one's weaknesses of direct floatation process that achieve cold crystallization, improve the manufacturing condition of former direct floatation process, make technique be easy to control, the Repone K rate of recovery brings up to 60%; Eliminate the Potassium Chloride Product that purity is 90%, Potassium Chloride Product purity is brought up to 93% ~ 95%; Horizontal stripes machine material water capacity is reduced to less than 15% by 20%, decreases bath water amount; Product granularity increases, output increased, and energy consumption of unit product reduces.On the whole, current cool technology is overcome by this invention---the system recoveries rate that direct floatation process exists is low, quality product not easily improves, product granularity is thin, not easily dehydration and dry shortcoming, Mineral resources have been saved in the raising of Repone K yield and the lifting of product grade, and energy-saving effect is obvious, has extensive dissemination.
Accompanying drawing explanation
Fig. 1 is that traditional cold is decomposed---direct floatation process schematic flow sheet;
Fig. 2 is the utility model system device connection diagram;
Fig. 3 is the utility model cold crystallization---direct floatation process schematic flow sheet.
Embodiment
In order to make the object, technical solutions and advantages of the present invention clearly, describe the present invention below in conjunction with the drawings and specific embodiments.
A kind of novel producing potassium chloride from carnallite production system and method are with salt-pan carnallite ore deposit be raw material production Potassium Chloride Product novel production system and technique.
Figure 2 shows that present system equipment connection schematic diagram, a kind of novel producing potassium chloride from carnallite production system, comprise and add ore deposit equipment, crystallizer, floatation equipment, filter plant, again plasm scouring equipment, centrifugal-dehydration device, dry packing equipment, each equipment is linked in sequence;
Increase crusher in described adding on the equipment of ore deposit, make larger carnallitite be able to fragmentation and diminish, be convenient to crystal system decomposition and crystallization;
Simultaneously in crystallizer, a kind of novel crystallization device (patent of invention number: ZL201310040807.3) of our company's invention is used to replace original cool technology---the carnallitite resolving device of direct floatation process, cool technology---in direct floatation process, cool technology system is by carnallitite hydrolyzable, due to key equipment---decompose the simple structure of tank, the residence time of carnallitite in decomposition tank is short, therefore Repone K does not have enough time to realize the increase of particle, and required decomposition amount of water is larger.The key equipment of cold crystallization system in the present invention---its tectonic division of novel crystallization device is negative area, dissolve area, region, three, race way, dissolve area is added above race way, extend the residence time of low-sodium carnalite in this region, make mixing evenly, reaction is more abundant, carnallitite reaches and decomposes completely; Owing to adding sedimentation crystallizing field volume, the Repone K after decomposition has time enough to grow up in crystallizing field; The ring-type mother liquor distributor that novel crystallization device is arranged around inner core pyramidal structure lower port, increase the contact area of mother liquor and low-sodium carnalite, be issued to the effect of abundant mixed decomposition at the stirring action of ejection liquid simultaneously, solve crystallizer in the past fully mixed decomposition just by the overflow of inner core top to the problem of crystalliser feet; Novel crystallization device height reduction, shortens stir shaft, improves stirrer operation stability, deduct stir shaft plummer-block simultaneously, reduce the fault point simultaneously, increases crystallizer continuous operating time, plays essence ensure the single tank production capacity of raising; CFD and FEA technology is have employed in tank body and stirrer design, field of flow and tank structure are optimized, decomposition reaction district scope is adjusted, increase the decomposition reaction district residence time, be beneficial to decomposition reaction fully to carry out, meet carnallitite decomposition and crystallization demand.Add sedimentation crystallizing field volume, actually increase output, reduce unit output energy consumption.
The production method of described novel producing potassium chloride from carnallite system, concrete technology is as follows:
Add ore deposit: the carnallitite that system is shone in salt pan is transported in crude ore bin by gathering, adjust upper ore deposit amount through spiral and be transported to reciprocating sieve, crusher is entered after nugget larger in raw ore and other foreign material sieves being removed, crusher by crushing raw ore to below 20mm, be convenient to decomposition and the crystallization effect of crystallizer, carnallite after fragmentation is transported to crystallizer, carries out decomposition and crystallization;
Crystallization: the smart potassium mother liquor that the carnallite after described fragmentation and centrifugation systems produce, decompose fresh water and enter crystallizer, because of KCl, NaCl, MgCl simultaneously
2different solubility, MgCl
2first dissolve completely and be present in crystallizer with liquid form, KCl continues to dissolve formation KCl saturated solution, and along with the continuous increase adding ore deposit amount, KCL forms supersaturated solution crystallization.NaCl can not separate out liquid phase is unsaturated, and tiny NaCl dissolves and major part exists with solid phase particles form.Therefore complete the decomposition of carnallitite in crystallizer, increase Repone K grain size number simultaneously;
Flotation: the slurry pipeline transport after decomposition and crystallization is to the medicament mediation groove of floatation system, the flotation reagent added with floatation system metering chemical feeding device carries out being in harmonious proportion rear gravity flow and enters flotation machine, flotation operation adopts one roughing, recleaning, once purging selection, obtains thick potassium slip through flotation.Wherein selected froth product is from flowing to filtering system, and the filtrate after filtration is high mother liquid of magnesium, and carry out circulation and be used for regulating selected operation concentration, all the other deliver to tail salt pond by mine tailing;
Filter, plasm scouring, centrifuge dehydration again: after the horizontal stripes machine of the described thick potassium slip from floatation system system after filtration removes high mother liquid of magnesium, add fresh water in the wash agitation groove of plasm scouring system again, the magnesium chloride of removing absorption and sodium-chlor wherein.Slip whizzer after washing removes washing mother liquor (smart potassium mother liquor), becomes smart potassium, is delivered to dehumidification system drying.Essence potassium mother liquor reclaims with being pumped to crystallizer and replacing a part of fresh water to decompose carnallite after flowing to smart potassium mother liquor tank;
Dry, packaging: described from the smart potassium after centrifuge dewatering by Belt Conveying to whizzer, the hot blast by burning in drying machine carries out drying.Dried product is packed to wrapping machine by belt haulage.
Accompanying drawing 3 is shown in above technical process.
Direct floatation process compares cold crystallization---direct floatation process and cool technology---, carnallitite through broken with smart potassium mother liquor, decompose fresh water and enter crystallizer diversion district simultaneously, when controlling ore deposit amount, amount of water, underflow flow, stirring frequency well, be beneficial to and improve manufacturing condition, increase product K Cl granularity; Capacity of decomposition can be made effectively to be increased, improve and decompose Repone K yield; Along with the increase of KCl granularity, flotation three phase boundary is more stable, and sorting result is obvious, while raising flotation operation index, improves potassium yield.The increase of KCl granularity, be beneficial to horizontal stripes machine and centrifuge dewatering, water capacity reduces relatively, alleviates the difficulty of washing, and drying cost can be made to reduce, and product index is easy to control, and energy consumption of unit product reduces.
Claims (1)
1. a novel producing potassium chloride from carnallite production system, is characterized in that, comprise and add ore deposit equipment, crystallizer, floatation equipment, filter plant, again plasm scouring equipment, centrifugal-dehydration device, dry packing equipment, each equipment is linked in sequence; Increase crusher in described adding on the equipment of ore deposit, be convenient to crystal system decomposition and crystallization; Simultaneously in described crystallizer, use the carnallitite resolving device of direct floatation process, the tectonic division of described novel crystallization device is negative area, dissolve area, region, three, race way, dissolve area is added above race way, extend the residence time of low-sodium carnalite in this region, make mixing evenly, reaction is more abundant, carnallitite reaches and decomposes completely; Add sedimentation crystallizing field volume, the Repone K after decomposition has time enough to grow up in crystallizing field; The ring-type mother liquor distributor that novel crystallization device is arranged around inner core pyramidal structure lower port, increases the contact area of mother liquor and low-sodium carnalite; CFD and FEA technology is have employed in tank body and stirrer design.
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107739037A (en) * | 2017-11-16 | 2018-02-27 | 中国科学院青海盐湖研究所 | A kind of method that carnallite prepares big particle diameter potassium chloride |
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| CN107739037A (en) * | 2017-11-16 | 2018-02-27 | 中国科学院青海盐湖研究所 | A kind of method that carnallite prepares big particle diameter potassium chloride |
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| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150107 Termination date: 20160710 |
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