CN108714332A - Molybdenum concntrate dewatering system - Google Patents
Molybdenum concntrate dewatering system Download PDFInfo
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- CN108714332A CN108714332A CN201810765460.1A CN201810765460A CN108714332A CN 108714332 A CN108714332 A CN 108714332A CN 201810765460 A CN201810765460 A CN 201810765460A CN 108714332 A CN108714332 A CN 108714332A
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- molybdenum concntrate
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
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Abstract
The invention discloses a kind of molybdenum concntrate dewatering systems, molybdenum concntrate dewatering system includes enrichment facility, filter device, drying device and collection device, enrichment facility is used to the ore pulp solution containing molybdenum concntrate being concentrated into setting concentration, filter device is connected with enrichment facility, filter device is used to set the ore pulp solution filtering of concentration, isolate filter cake and filtrate, filter device has the return duct that filtrate is back to enrichment facility, drying device is connected with filter device, drying device receives the filter cake that filter device is isolated, and filter cake is dried, collection device is connected with drying device to collect the filter cake after drying.Molybdenum concntrate dewatering system according to the ... of the embodiment of the present invention realizes the integrated process for filtering, drying and transporting and the configuration of material, reduces intermediate transport, has bad luck and store link, greatly improves dehydration efficiency.It is lost caused by filtering, drying in addition, also reducing fine fraction molybdenum concntrate, ensure that molybdenum concntrate effectively recycles.
Description
Technical field
The present invention relates to nonferrous metal mine technical field more particularly to a kind of molybdenum concntrate dewatering systems.
Background technology
In the ore dressing plant of nonferrous metal mine, molybdenum concntrate can be used as a kind of product of Beneficiation flowsheet after dehydration
The molybdenums converted products raw material such as subsequent production molybdenum-iron, ammonium molybdate.Molybdenum concntrate is generally flotation operation product, in order to obtain qualified molybdenum essence
Mine, it usually needs carry out fine grinding, cause molybdenum concntrate product cut size thin, it is not easy to be dehydrated, and subsequent production is to molybdenum concntrate
Moisture and oil content are high, and usual dewatering process is three sections.Country's molybdenum concntrate dewatering process is mostly three stage dewatering technologies at present, i.e., dense
Contracting+filtering+drying, the final qualified molybdenum concntrate for obtaining grease content < 4%.It is domestic in order to meet the requirement of final molybdenum concntrate
The Main Tissues form of three stage dewatering technology of molybdenum concntrate is that concentration operation uses common thickener, filtration operation to mostly use press filtration
Machine, vacuum drum filter etc., drying operation mostly use electric furnace, electromagnetical spiral drying machine, Rotatingandflashstreamingdrier, steam spiral
Drying machine etc..Vacuum drum filter has been cited as high energy consumption obsolete product and is forbidden to use at present.The molybdenum essence of extensive utilization at present
It is high that three stage dewatering technology of mine is generally faced with entire process energy consumption, especially filtering and drying operation high energy consumption, at the same filter and
Drying operation is mostly to operate intermittently, and product storage bin or other storage facilities is needed to be connected between two operations, inconvenient for operation, behaviour
Workmanship's labor intensity is big, and molybdenum concntrate drying loss is serious, and operating environment is poor.
The moral molybdenum ore day in small city season of the prior art handles 25000 tons of molybdenum ore project molybdenum concntrates and uses three sections of dewatering process flows,
One section be concentration, two sections be press filtration, three sections be drying, through GX-6 high-efficiency concentrators concentration, 200m2Filter press press filtration, WH85-A
Concentrate aqueous 2%~4% after the three sections of dehydrations of hollow slurries drying machine, drying.
Yichun deer ring molybdenum ore mining area of the prior art is a super-huge Molybdenum Mine.The major product in ore dressing plant is molybdenum essence
Powder, byproduct are powdered copper concentrate and sulphur fine powder.The design comminution flow is crushed+ball milling flow using Semi-Autogenous+hard rock.Molybdenum concntrate is adopted
With dense+three stage dewatering technology flow of press filtration+drying, moisture in concentrate 4%；Copper concentrate uses dense+press filtration two-stage dewatering technique
Flow, moisture in concentrate 12%；Iron concentrate is using dense+filtering two-stage dewatering technological process, moisture in concentrate 12%.
In the prior art, Baihualing Concentrator is one of two ore dressing plants of Jinduicheng Aluminium Industry Group Co., Ltd subordinate.
Molybdenum concntrate has obtained grade 52% by concentration, filtering, dry three sections of dehydrations, it is aqueous be less than 8% molybdenum concntrate.
In the prior art, Baihualing Concentrator molybdenum concntrate in the cities Jin Dui is taken using concentration-press filtration two-stage dewatering new technological flow
It is dehydrated old technological process for concentration-three sections of filtering-drying, final molybdenum concntrate moisture content is less than 10%, solves high-quality fine fraction
The dehydration problem of molybdenum concntrate.Compared with old technology, the environmental pollution that drying operation is brought is completely eliminated, significantly energy saving drop
Consumption.
In the prior art, copper-molybdenum ore-sorting system intrinsic molybdenum concntrate dehydration process in Shouwangfen Copper Mine ore dressing plant uses
Three sections of dehydrations, i.e., flotation molybdenum concentrate feeds incline board concentrating box, and overflow is precipitated through two sections of sedimentation basins, and primary water discards, precipitation
Object periodically recycling is given to drying operation, and output moisture is less than 4% molybdenum concntrate powder.Improved flow uses two-stage dewatering, i.e.,
Flotation molybdenum concentrate feeds concentrator, without filtering directly to entering helicoid screw dryer, coal-fired heating, it is dry after molybdenum concntrate from drying
Machine gape is discharged, and concentrator overflow water is after two sections of sedimentation basins precipitate, and primary water discards, and sediment periodically manually digs out and feeds
Drying machine is dried again, the molybdenum concntrate powder of output qualification.
In the above prior art, the prior art 1 and the prior art 2 are all made of concentration+three sections of press filtration+drying dehydration and make
Industry, press filtration operation are interruption operation, and ore discharge needs transporting equipment to be connected with drying operation, and buffer-stored is needed to set
It applies.The prior art 3 is using using concentration+three sections of filtering+drying dehydration, and filtering is using superseded drum vacuumfilter energy consumption
Height needs conveying equipment to be connect with drying machine, and drying machine dust is big, and loss is serious, and environment is poor；The prior art 4 is de- using two sections
Hydraulic art, final molybdenum concntrate moisture fail the requirement for reaching subsequent production molybdenum-iron product, need subsequently to increase drying operation；It is existing
Technology 5 uses concentration+drying two-stage dewatering operation, and since the concentration underflow density control for entering dry is limited, water content is high,
Energy consumption for drying is high, whole high energy consumption.
In conclusion carried out numerous studies for molybdenum concntrate dewatering process both at home and abroad, including different filter plants with
Drying equipment is tested and use research, but high to molybdenum concntrate dehydration energy, and operation is discontinuous, and labor intensity is big, operation
Environment is poor, and molybdenum concntrate dewatering operation loss serious problems, which are not given fundamentally, to be solved.
Invention content
The present invention is directed at least solve one of the technical problems existing in the prior art.For this purpose, the present invention proposes a kind of molybdenum
Essence mine dehydration system, the molybdenum concntrate dewatering system energy consumption is relatively low, and operation is continuous, and molybdenum concntrate loss is smaller.
Molybdenum concntrate dewatering system according to the ... of the embodiment of the present invention, including：Enrichment facility, the enrichment facility will be for that will contain
The ore pulp solution of molybdenum concntrate is concentrated into setting concentration；Filter device, the filter device are connected with the enrichment facility, the mistake
Filter device is used to set the ore pulp solution filtering of concentration, isolates filter cake and filtrate, and the filter device has will
The filtrate is back to the return duct of the enrichment facility；Drying device, the drying device are connected with the filter device, institute
It states drying device and receives the filter cake that the filter device is isolated, and the filter cake is dried；Collection device, it is described
Collection device is connected with the drying device to collect the filter cake after drying；Wherein：The filter device will set it is dense
The solution of degree is filtered during being transported towards the drying device；The drying device is by the filter cake direction
It is dried during the collection device transport.
Molybdenum concntrate dewatering system according to the ... of the embodiment of the present invention, since filter device is dry in the solution direction that will set concentration
It is filtered during dry device transport, drying device is dried during transporting filter cake towards collection device.
The seamless connection for realizing filter device and drying device is realized the integrated process for filtering, drying and transporting of material and is matched
It sets, reduces intermediate transport, has bad luck and store link, greatly improve dehydration efficiency.It will be filtered further, since filter device has
Liquid is back to the return duct of enrichment facility, that is to say, that the filtrate that filter device is isolated will return to thickener, reduce particulate
Grade molybdenum concntrate loses caused by filtering, ensure that molybdenum concntrate effectively recycles.
In some embodiments, the molybdenum concntrate dewatering system further includes：Agitating device, the agitating device are located at
Between the enrichment facility and the filter device, the agitating device is for stirring evenly the solution.
In some embodiments, the molybdenum concntrate dewatering system further includes：Homogenizing device, the homogenizing device are located at
Between the enrichment facility and the filter device, the homogenizing device is used to the solution being equably laid on the filtering
On device.
In some embodiments, the molybdenum concntrate dewatering system further includes：Pulp pump, the Pulp pump are located at described
Between enrichment facility and the filter device.
In some embodiments, the molybdenum concntrate dewatering system, the drying device include：Drying box, the drying
Drying chamber and steam channel spaced apart are limited in case, the drying chamber has inlet and outlet, the import and the mistake
It filters device to be connected, the outlet is connected with the collection device；Delivery section, the delivery section is located in the drying box, described
Delivery section is for conveying the filter cake of the entrance towards the outlet.
Specifically, the steam channel is at least partially formed in the delivery section.
In some embodiments, the drying device is helicoid screw dryer.
In some embodiments, the filter device includes：Filter bag, the filter bag is for filtering the solution；It is more
A belt wheel, the multiple belt wheel are connected with the filter bag to drive the filter bag to move；Liquid holding box, the liquid holding box are located at
The lower section of the filter bag, the return duct are connected with the liquid holding box.
In some optional embodiments, the filter device is vacuum band-type filter machine.
In some embodiments, the enrichment facility includes：Concentrate case, the concentration case with stoste outflow, filtrate into
Mouth, taphole and water outlet, the stoste outflow, the filtrate import and the water outlet are located at the top of the concentration case
Portion, the taphole are located at the bottom of the concentration case, and the filtrate import is connected with the return duct.
The additional aspect and advantage of the present invention will be set forth in part in the description, and will partly become from the following description
Obviously, or practice through the invention is recognized.
Description of the drawings
The above-mentioned and/or additional aspect and advantage of the present invention will become in the description from combination following accompanying drawings to embodiment
Obviously and it is readily appreciated that, wherein：
Fig. 1 is the overall structure figure of molybdenum concntrate dewatering system according to embodiments of the present invention.
Fig. 2 is the dehydration figure of molybdenum concntrate dewatering system according to the ... of the embodiment of the present invention.
Reference numeral：
Molybdenum concntrate dewatering system 100,
Enrichment facility 110,
Stoste outflow 111, filtrate import 112, taphole 113, water outlet 114,
Filter device 120,
Return duct 121, liquid holding box 122, belt wheel 123, filter bag 124
Drying device 130,
Drying box 131, drying chamber 1311, steam channel 1312, delivery section 132,
Collection device 140,
Agitating device 150,
Homogenizing device 160,
Pulp pump 170.
Specific implementation mode
The embodiment of the present invention is described below in detail, examples of the embodiments are shown in the accompanying drawings, wherein from beginning to end
Same or similar label indicates same or similar element or element with the same or similar functions.Below with reference to attached
The embodiment of figure description is exemplary, and is only used for explaining the present invention, and is not considered as limiting the invention.
In the description of the present invention, it is to be understood that, term "center", " longitudinal direction ", " transverse direction ", " length ", " width ",
" thickness ", "upper", "lower", "front", "rear", "left", "right", "vertical", "horizontal", "top", "bottom" "inner", "outside", " up time
The orientation or positional relationship of the instructions such as needle ", " counterclockwise ", " axial direction ", " radial direction ", " circumferential direction " be orientation based on ... shown in the drawings or
Position relationship is merely for convenience of description of the present invention and simplification of the description, and does not indicate or imply the indicated device or element must
There must be specific orientation, with specific azimuth configuration and operation, therefore be not considered as limiting the invention.In addition, limit
There is the feature of " first ", " second " to can explicitly or implicitly include one or more this feature surely.The present invention's
In description, unless otherwise indicated, the meaning of " plurality " is two or more.
In the description of the present invention, it should be noted that unless otherwise clearly defined and limited, term " installation ", " phase
Even ", " connection " shall be understood in a broad sense, for example, it may be being fixedly connected, may be a detachable connection, or be integrally connected；It can
Can also be electrical connection to be mechanical connection；It can be directly connected, can also indirectly connected through an intermediary, Ke Yishi
Connection inside two elements.For the ordinary skill in the art, above-mentioned term can be understood at this with concrete condition
Concrete meaning in invention.
Molybdenum concntrate dewatering system 100 according to the ... of the embodiment of the present invention is described below with reference to Fig. 1.
As shown in Figure 1, molybdenum concntrate dewatering system 100 according to the ... of the embodiment of the present invention includes enrichment facility 110, filter device
120, drying device 130 and collection device 140.Enrichment facility 110 is used to the ore pulp solution containing molybdenum concntrate being concentrated into setting
Concentration, filter device 120 are connected with enrichment facility 110, and filter device 120 is used to set the ore pulp solution filtering of concentration, divides
Filter cake and filtrate are separated out, filter device 120 has the return duct 121 that filtrate is back to enrichment facility 110, drying device
130 are connected with filter device 120, and drying device 130 receives the filter cake that filter device 120 is isolated, and filter cake is dried,
Collection device 140 is connected with drying device 130 to collect the filter cake after drying.Filter device 120 is in the solution that will set concentration
It is filtered during being transported towards drying device 130, drying device 130 is transporting filter cake towards collection device 140
It is dried in the process.
It should be noted that in the dehydration of molybdenum concntrate, filter device 120 is dry in the solution direction that will set concentration
Device 130 is filtered during transporting, that is to say, that filter device 120 carries out solution during conveying solution
Filtering.Therefore, the filter device 120 of molybdenum concntrate of embodiment of the present invention dewatering system 100 serves not only as filter dewatering equipment, simultaneously
It as the transporting equipment of material, carries out the transport of material and has bad luck, and it is continuous to work.Compared with the filter plant of the prior art,
The filter device 120 of the embodiment of the present invention eliminates the additional conveying equipment of filter cake, while reducing the storage between subsequent job
It deposits facility and such as stores funnel, storage silo etc..At the same time, filtrate is back to enrichment facility since filter device 120 has
110 return duct 121, that is to say, that the filtrate that filter device 120 is isolated will return to thickener, reduce fine fraction molybdenum essence
Mine is lost caused by filtering, ensure that molybdenum concntrate effectively recycles.
In addition, in the dehydration of molybdenum concntrate, drying device 130 is in the process for transporting filter cake towards collection device 140
In be dried.That is, drying device 130 dries filter cake during conveying filter cake.Therefore, of the invention
The drying device 130 of embodiment molybdenum concntrate dewatering system 100 serves not only as drying equipment, while as the transporting equipment of material,
It is done directly the transport of material and has bad luck, and it is continuous to work.Compared with the drying equipment of the prior art, the embodiment of the present invention is done
Dry device 130 eliminates the conveying equipment after drying, can directly discharge the filter cake after drying in collection device 140.
Molybdenum concntrate dewatering system 100 according to the ... of the embodiment of the present invention, since filter device 120 is in the solution that will set concentration
It is filtered during being transported towards drying device 130, drying device 130 is transporting filter cake towards collection device 140
It is dried in the process.The seamless connection for realizing filter device 120 and drying device 130, realize the filtering of material, dry and
The integrated process of transport and configuration reduce intermediate transport, have bad luck and store link, greatly improve dehydration efficiency.In addition,
Since filter device 120 has the return duct 121 that filtrate is back to enrichment facility 110, that is to say, that filter device 120 detaches
The filtrate gone out will return to thickener, reduce fine fraction molybdenum concntrate and lost caused by filtering, ensure that molybdenum concntrate effectively recycles.
In some embodiments, molybdenum concntrate dewatering system 100 further includes agitating device 150, and agitating device 150 is located at concentration
Between device 110 and filter device 120, agitating device 150 is for stirring evenly solution.It is understood that agitating device
150 pairs of ore pulp solution containing molybdenum concntrate are delivered to filter device 120 again after stirring evenly, and thereby ensure that into filter device
120 solution is more uniform, to improve the filter effect of filter device 120.It should be noted that agitating device 150 is only right
Solution is stirred effect, therefore does not make limitation to the concrete type of agitating device 150 herein, that is to say, that agitating device
150 can be any device that can play stirring action.
In some embodiments, molybdenum concntrate dewatering system 100 further includes homogenizing device 160, and homogenizing device 160 is located at concentration
Between device 110 and filter device 120, solution for being equably laid on filter device 120 by homogenizing device 160.It can be with
Understand, homogenizing device 160 ensure that solution is evenly distributed on filter device 120 so that filter cake is separated to come through filtering
Afterwards, filter cake thickness is moderate, and filter effect is ideal.It should be noted that homogenizing device 160 only carries out uniformly distributed effect to solution, because
This does not make limitation to the concrete type of homogenizing device 160 herein, that is to say, that homogenizing device 160 can play to be any
The device of uniformly distributed solution effects.
Advantageously, in the embodiment having, molybdenum concntrate dewatering system 100 includes agitating device 150 and homogenizing device 160,
And in the direction of motion of solution, homogenizing device 160 is located at the downstream of agitating device 150.Thus, it is possible to better ensure that filtering
The filter effect of device 120.
In some embodiments, molybdenum concntrate dewatering system 100 further includes Pulp pump 170, and Pulp pump 170 is located at enrichment facility
Between 110 and filter device 120.It is understood that Pulp pump 170 provides power for solution, it ensure that solution can be compared with
To be easy to transport to filter device 120 from enrichment facility 110, avoids solution and natural subsidence occurs in flow process to make
It obtains molybdenum concntrate and deposits to the transport pipeline between enrichment facility 110 and filter device 120.
In some embodiments, drying device 130 includes drying box 131 and delivery section 132, is defined in drying box 131
Drying chamber 1311 and steam channel 1312 spaced apart, drying chamber 1311 have inlet and outlet, import and 120 phase of filter device
Even, outlet is connected with collection device 140, and delivery section 132 is located in drying box 131, and delivery section 132 is used for the filter cake of entrance
Towards outlet conveying.It is understood that in the drying process, filter cake is delivered to outlet by delivery section 132 by import, is being conveyed
The steam with higher heat passes through in steam channel 1312 in the process, it is possible thereby to complete the drying to filter cake.Obviously
, for the steam of high temperature there is no being in direct contact with filter cake, the mode of this contact drying is not likely to produce powder in the drying process
Dirt reduces dry caused molybdenum concntrate loss.
Certainly, it should be noted that delivery section 132 can there are many forms, such as delivery section 132 can be formed as conveying
Spiral can also be formed as conveyer belt, may be formed as other forms.
Specifically, steam channel 1312 is at least partially formed in delivery section 132.Thus, it is possible to reduce drying device 130
Size.Certainly, it steam channel 1312 and can be fully located at outside delivery section 132.
In some embodiments, drying device 130 is helicoid screw dryer.Certainly, drying device 130 can also be dry for other
Dry machine, does not enumerate explanation herein.
In some embodiments, filter device 120 includes filter bag 124 and multiple belt wheels 123 and liquid holding box 122, filtering
Band 124 is used for filtering solution, and multiple belt wheels 123 are connected with filter bag 124 to drive filter bag 124 to move, and liquid holding box 122 is located at
The lower section of filter bag 124, return duct 121 are connected with liquid holding box 122.It is understood that when ore pulp solution enters filter bag 124
When upper, filter bag 124 is filtered and conveys to ore pulp solution, and the filtrate that solution is separated is by the mistake on filter bag 124
Filter opening falls into liquid holding box 122 and enters enrichment facility 110 by return duct 121, and filter cake stays on filter bag 124 and by filter bag
124 are delivered to drying device 130.In conclusion filter device 120 has carried out mistake during transfer ore pulp solution to solution
Filter.That is, filter device 120 serves not only as filter dewatering equipment, while as the transporting equipment of material, carrying out material
It transports and has bad luck, and it is continuous to work.Compared with the filter plant of the prior art, the filter device 120 of the embodiment of the present invention is cancelled
The additional conveying equipment of filter cake, while the storage facility reduced between subsequent job such as stores funnel, storage silo etc..With
This is simultaneously as filter device 120 has the return duct 121 that filtrate is back to enrichment facility 110, that is to say, that filter device
120 filtrates isolated will return to thickener, reduce fine fraction molybdenum concntrate and lost caused by filtering, ensure that molybdenum concntrate has
Effect recycling.
In some optional embodiments, filter device 120 is vacuum band-type filter machine.Certainly, filter device 120 may be used also
Think other filters, does not illustrate herein.
In some embodiments, enrichment facility 110 includes concentration case, and concentration case has stoste outflow 111, filtrate import
112, taphole 113 and water outlet 114, stoste outflow 111, filtrate import 112 and water outlet 114 are located at the top of concentration case
Portion, taphole 113 are located at the bottom of concentration case, and filtrate import 112 is connected with return duct 121.It is understood that stoste with
Filtrate constitutes the ore pulp solution containing molybdenum concntrate, and is concentrated to it by enrichment facility 110.
In some embodiments, stoste and the ore pulp solution concentration containing molybdenum concntrate of filtrate composition are 25%~30%
Solution, conveys by pump or flow to certainly the enrichment facility 110 for being formed as common thickener, and common thickener is added without flocculant and filled
It sets, common thickener side is equipped with foam baffle, and periphery is equipped with the foamite system that disappears of spraying water, and molybdenum concntrate obtains underflow by natural subsidence
50% molybdenum concntrate solution of concentration.
Below with reference to the molybdenum concntrate dewatering system 100 of Fig. 1-Fig. 2 descriptions specific embodiment of the invention.
The molybdenum concntrate dewatering system 100 of the present embodiment include enrichment facility 110, filter device 120, agitating device 150,
Expect device 160, Pulp pump 170, drying device 130 and collection device 140.Enrichment facility 110 will be for that will contain the mine of molybdenum concntrate
Slurry solution is concentrated into setting concentration, and filter device 120 is connected with enrichment facility 110, and filter device 120 will be for that will set concentration
Filter cake and filtrate are isolated in the filtering of ore pulp solution, and filter device 120 has the reflux that filtrate is back to enrichment facility 110
Pipe 121.Filter device 120 is formed as rubber vacuum band filter.Drying device 130 is connected with filter device 120, dry dress
The filter cake that 130 reception filter devices 120 are isolated is set, and filter cake is dried, drying device 130 is formed as spiral drying
Machine.Collection device 140 is connected with drying device 130 to collect the filter cake after drying.Filter device 120 will set the molten of concentration
Liquid is filtered during being transported towards drying device 130；Drying device 130 is transporting filter cake towards collection device 140
During be dried.Agitating device is located between enrichment facility 110 and filter device 120, and agitating device 150 is used for will be molten
Liquid stirs evenly, and agitating device 150 is formed as stirred tank, and Pulp pump 170 is located between agitating device 150 and filter device 120,
Homogenizing device 160 is located between Pulp pump 170 and filter device 120, and homogenizing device 160 is formed as homocline mine case, homogenizing device
160 for solution to be equably laid on to filter device 120.
The molybdenum concntrate dewatering system 100 of the present embodiment is fully sent out by selecting suitable concentration, filtering and drying equipment
The characteristics of waving three classes equipment and advantage finally realize the reasonable distribution of dewatering process parameter between equipment, especially water content
The reasonable distribution of removing, the final final goal for realizing low energy consumption dehydration.At the same time, filtering has also been given full play to, drying is set
Standby continuous type feature, realizes the integrated process for filtering, drying and transporting and the configuration of material, reduces intermediate fortune
It is defeated, have bad luck and store link, greatly improve dehydration efficiency.In addition, on the basis of working continuously, drying device 130 is realized
The totally-enclosed operation of material, on the one hand reduces the loss of molybdenum concntrate, on the other hand improves operating environment, reduces work labour
Intensity, operation are more convenient convenient.
The molybdenum concntrate dewatering process of the molybdenum concntrate dewatering system 100 of the present embodiment includes the following steps：
(1) it low concentration is contained into molybdenum concntrate solution is delivered to enrichment facility 110 and carry out concentration primary dewatering, it is molten after concentration
Liquid a concentration of 50%；
(2) solution after concentration is buffered from stirred tank is flow to, and is stirred 3-5 minutes in stirred tank, then through slag
Stock pump 170 is delivered to homocline mine case；
(3) homocline mine case is by molybdenum concntrate ore pulp uniform distribution to rubber vacuum band filter, rubber vacuum belt type filter
Machine is filtered second dehydration, and the moisture of filtered filter cake is 18%~20%；
(4) filtrate generated after the filtering of rubber vacuum band filter is back to concentration dress by the gravity flow of return duct 121
Set 110；
(5) triple dewatering is dried by transport to the helicoid screw dryer of rubber vacuum band filter in filter cake, dry
Molybdenum concntrate grease content < 4% afterwards.
(6) filter cake after helicoid screw dryer drying is transported through helicoid screw dryer, is emitted into the collection for storing filter cake and is filled
It sets in 140.
The dewatering process of the molybdenum concntrate dewatering system 100 of the present embodiment has the following advantages compared with prior art：
(1) concentration+filtering+drying triple dewatering is used, molybdenum concntrate dehydration efficiency is improved, it is final to realize molybdenum concntrate grease
Content < 4%；
(2) loss in molybdenum concntrate dehydration is effectively reduced, enrichment facility is back to by 120 filtrate of filter device
110, drying device 130 realizes that filter cake is completely enclosed using indirect type steam heating coil drying machine, is not likely to produce dust etc. and arranges
It applies, reduces filtering, dry caused loss；
(3) rubber vacuum band filter+helicoid screw dryer integration of operation is used, realizes that filtering and drying operation are continuous,
The transporting equipment and intermediate storage for cancelling filter cake, greatly improve the operational efficiency of dehydration, reduce cost；
(4) it filters and drying is worked continuously, reduce the interruption number of helicoid screw dryer heat supply, improve the running rate of equipment,
Reduce entire dehydration procedure energy consumption and operating cost；
(5) rubber vacuum band filter ensures that molybdenum concntrate moisture 18%~20%, helicoid screw dryer closed operation reduce
Dust improves operating environment, reduces labor intensity.
In the description of this specification, reference term " one embodiment ", " some embodiments ", " illustrative examples ",
The description of " example ", " specific example " or " some examples " etc. means specific features described in conjunction with this embodiment or example, knot
Structure, material or feature are included at least one embodiment or example of the invention.In the present specification, to above-mentioned term
Schematic representation may not refer to the same embodiment or example.Moreover, specific features, structure, material or the spy of description
Point can be combined in any suitable manner in any one or more of the embodiments or examples.
Although an embodiment of the present invention has been shown and described, it will be understood by those skilled in the art that：Not
In the case of being detached from the principle of the present invention and objective a variety of change, modification, replacement and modification can be carried out to these embodiments, this
The range of invention is limited by claim and its equivalent.
Claims (10)
1. a kind of molybdenum concntrate dewatering system, which is characterized in that including：
Enrichment facility, the enrichment facility are used to the ore pulp solution containing molybdenum concntrate being concentrated into setting concentration；
Filter device, the filter device are connected with the enrichment facility, and the filter device will be for that will set the described of concentration
Ore pulp solution filtering isolates filter cake and filtrate, and the filter device has is back to the enrichment facility by the filtrate
Return duct；
Drying device, the drying device are connected with the filter device, and the drying device receives the filter device separation
The filter cake gone out, and the filter cake is dried；
Collection device, the collection device are connected with the drying device to collect the filter cake after drying；
Wherein：The filter device carried out during transporting the solution for setting concentration towards the drying device
Filter；The drying device is dried during transporting the filter cake towards the collection device.
2. molybdenum concntrate dewatering system according to claim 1, which is characterized in that further include：Agitating device, the stirring dress
It is set between the enrichment facility and the filter device, the agitating device is for stirring evenly the solution.
3. molybdenum concntrate dewatering system according to claim 1, which is characterized in that further include：Homogenizing device, the homocline dress
It is set between the enrichment facility and the filter device, the homogenizing device is used to the solution being equably laid on institute
It states on filter device.
4. molybdenum concntrate dewatering system according to claim 1, which is characterized in that further include：Pulp pump, the Pulp pump are set
Between the enrichment facility and the filter device.
5. molybdenum concntrate dewatering system according to claim 1, which is characterized in that the drying device includes：
Drying box, drying chamber and steam channel spaced apart are limited in the drying box, and the drying chamber has import and goes out
Mouthful, the import is connected with the filter device, and the outlet is connected with the collection device；
Delivery section, the delivery section are located in the drying box, and the delivery section is used for the filter cake court of the entrance
It is conveyed to the outlet.
6. molybdenum concntrate dewatering system according to claim 5, which is characterized in that the steam channel is at least partially formed in
In the delivery section.
7. molybdenum concntrate dewatering system according to claim 1, which is characterized in that the drying device is helicoid screw dryer.
8. molybdenum concntrate dewatering system according to claim 1, which is characterized in that the filter device includes：
Filter bag, the filter bag is for filtering the ore pulp solution；
Multiple belt wheels, the multiple belt wheel are connected with the filter bag to drive the filter bag to move；
Liquid holding box, the liquid holding box are located at the lower section of the filter bag, and the return duct is connected with the liquid holding box.
9. molybdenum concntrate dewatering system according to claim 1, which is characterized in that the filter device is vacuum belt filter
Machine.
10. molybdenum concntrate dewatering system according to claim 1, which is characterized in that the enrichment facility includes：Case is concentrated,
The concentration case have stoste outflow, filtrate import, taphole and water outlet, the stoste outflow, the filtrate import and
The water outlet is located at the top of the concentration case, and the taphole is located at the bottom of the concentration case, the filtrate import
It is connected with the return duct.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810765460.1A CN108714332A (en) | 2018-07-12 | 2018-07-12 | Molybdenum concntrate dewatering system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201810765460.1A CN108714332A (en) | 2018-07-12 | 2018-07-12 | Molybdenum concntrate dewatering system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108714332A true CN108714332A (en) | 2018-10-30 |
Family
ID=63914143
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201810765460.1A Pending CN108714332A (en) | 2018-07-12 | 2018-07-12 | Molybdenum concntrate dewatering system |
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| CN (1) | CN108714332A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109276947A (en) * | 2018-11-13 | 2019-01-29 | 中国北方稀土（集团）高科技股份有限公司 | The device and method being separated by solid-liquid separation in carbonated rare earth continuous production |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201050931Y (en) * | 2007-06-12 | 2008-04-23 | 杨东波 | Metallic ore fine powder dryer |
| CN102631978A (en) * | 2012-03-30 | 2012-08-15 | 洛阳栾川钼业集团股份有限公司 | Method free from pickling dephosphorization for wolframine wet concentrate |
| CN202860276U (en) * | 2012-09-20 | 2013-04-10 | 云南华联锌铟股份有限公司 | Tin concentrate dewatering combination equipment |
| CN204672006U (en) * | 2015-05-15 | 2015-09-30 | 张利军 | A kind of dry-discharge system for tailings |
| CN204999954U (en) * | 2015-10-12 | 2016-01-27 | 长沙有色冶金设计研究院有限公司 | Molybdenum concntrate dehydration system |
| CN208583088U (en) * | 2018-07-12 | 2019-03-08 | 中国恩菲工程技术有限公司 | Molybdenum concentrate dewatering system |
-
2018
- 2018-07-12 CN CN201810765460.1A patent/CN108714332A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201050931Y (en) * | 2007-06-12 | 2008-04-23 | 杨东波 | Metallic ore fine powder dryer |
| CN102631978A (en) * | 2012-03-30 | 2012-08-15 | 洛阳栾川钼业集团股份有限公司 | Method free from pickling dephosphorization for wolframine wet concentrate |
| CN202860276U (en) * | 2012-09-20 | 2013-04-10 | 云南华联锌铟股份有限公司 | Tin concentrate dewatering combination equipment |
| CN204672006U (en) * | 2015-05-15 | 2015-09-30 | 张利军 | A kind of dry-discharge system for tailings |
| CN204999954U (en) * | 2015-10-12 | 2016-01-27 | 长沙有色冶金设计研究院有限公司 | Molybdenum concntrate dehydration system |
| CN208583088U (en) * | 2018-07-12 | 2019-03-08 | 中国恩菲工程技术有限公司 | Molybdenum concentrate dewatering system |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109276947A (en) * | 2018-11-13 | 2019-01-29 | 中国北方稀土（集团）高科技股份有限公司 | The device and method being separated by solid-liquid separation in carbonated rare earth continuous production |
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