CN207086120U - The separation system of molybdenum bismuth is reclaimed in multi-metal sulfide - Google Patents
The separation system of molybdenum bismuth is reclaimed in multi-metal sulfide Download PDFInfo
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- CN207086120U CN207086120U CN201720296185.4U CN201720296185U CN207086120U CN 207086120 U CN207086120 U CN 207086120U CN 201720296185 U CN201720296185 U CN 201720296185U CN 207086120 U CN207086120 U CN 207086120U
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Abstract
The separation system of molybdenum bismuth is reclaimed in multi-metal sulfide, it is characterised in that its grinding mechanism connects with Task-size Controlling device, and the Task-size Controlling device includes screen cloth, and the lower section of screen cloth connects with weight activated switch；Weight activated switch is with the first operating position and so that the second operating position that the top of screen cloth and the feedback port of grinding mechanism are cut off for the top of screen cloth is connected with the feedback port of grinding mechanism；The loading hopper for being arranged at the grinding mechanism upstream is in inverted tetragonous cone table shape, and the left and right sides of its upper end can be with automatic turning, automatically reset lid provided with two, and this is covered with rotating shaft and counterweight；The lower end of loading hopper is provided with charging and exported, charging outlet and the charging inlet communication of the grinding mechanism.The utility model realizes non-cyanide flotation beneficiation reagent system, does not use cyanide inhibitor, avoids production pollution.
Description
Technical field
A kind of separation system that molybdenum bismuth is reclaimed in multi-metal sulfide is the utility model is related to, it uses non-cyanide flotation to select
Ore deposit regime of agent, belongs to technical field of beneficiation.
Background technology
Cyanide is inhibitor important in nonferrous metal sulfide mineral flotation, and the Exemplary inhibitors of zincblende, its energy
Effectively suppress pyrite, zincblende and chalcopyrite.A small amount of cyanide can suppress pyrite, and dosage is slightly larger just to be suppressed to dodge zinc
Ore deposit, dosage is some larger, can suppress copper sulfide mineral, but does not have inhibitory action to galena, so, lead-zinc, copper-lead,
The separation of the mineral such as copper-zinc, zinc-sulphur, cyanide are once widely used as selective depressant always.
But cyanide has severe toxicity, in view of the requirement of environmental mining protection, is carrying out find cyanide generation in recent years always
The research of articles for use simultaneously achieves many progress, mainly in terms of the minerals separations such as lead-zinc, copper-zinc, zinc-sulphur, and for molybdenum-
It is less in terms of bismuth separation, because current cyanide substitute is required for first adjusting ore pulp with lime, thus it have impact on returning for molybdenum
Receive index.
The separation of tungsten mines multi-metal sulfide uses cyanide as inhibitor, due to the complexity of separation process,
Still have to be continuing with cyanide as inhibitor.According to《State Council is on further strengthening the work that eliminates the backward production facilities
Notice》(promulgated by the State Council [2010] 7) requirement, according to national relevant laws, regulation,《Part industrial trade, which is eliminated, falls behind production technology
Equipment and product guidance list (sheet in 2010)》Regulation：Eliminate backward Non-ferrous minerals ore dressing and use bichromate or cyanogen
The requirement of the separating technology of the Severely poisonous reagents such as compound, therefore, there is an urgent need to a kind of ore dressing medicine of non-cyanide flotation recovery molybdenum bismuth in market
Agent system and corresponding separation system.
However, a kind of technical prejudice inertia in other words in the prior art be present, it is believed that returned in multi-metal sulfide
The separation operation for receiving molybdenum bismuth inherently should be in this way, be exactly that environment is poor, always nobody considers how to carry out green ore dressing how
Production efficiency is improved, how while product quality is ensured to improve economic benefit.More nobody considers how to realize
The integrated screening installation of molybdenum bismuth is reclaimed in multi-metal sulfide.
Utility model content
The purpose of this utility model is to provide a kind of separation system that molybdenum bismuth is reclaimed in multi-metal sulfide, and it is realized
A kind of beneficiation reagent system for non-cyanide flotation recovery molybdenum bismuth researched and developed for tungsten mines multi-metal sulfide, alternative cyanide
Multi-metal sulfide is sorted as inhibitor, and original cyanide floatation indicators can be reached.
Therefore, according to one side of the present utility model, there is provided a kind of point that molybdenum bismuth is reclaimed in multi-metal sulfide
Select system, it is characterised in that its grinding mechanism connects with Task-size Controlling device, and the Task-size Controlling device includes screen cloth, screen cloth
Lower section and weight activated switch connect；Weight activated switch, which has, makes the top of screen cloth be connected with the feedback port of grinding mechanism
The first operating position and cause screen cloth top and grinding mechanism feedback port cut-out the second operating position；It is arranged at described
The loading hopper of grinding mechanism upstream is in inverted tetragonous cone table shape, the left and right sides of its upper end be provided with two can with automatic turning,
Automatically reset lid, this is covered with rotating shaft and counterweight；The lower end of loading hopper be provided with charging export, the charging outlet with it is described
The charging inlet communication of grinding mechanism.
Preferably, the separation system also includes size mixing priming apparatus, inhibitor lime adding set, the addition of capturing agent kerosene
Device, capturing agent diethyldithiocarbamate adding set, capturing agent Z-200 adding sets, foaming agent vulcanized sodium adding set.
According to another aspect of the present utility model, there is provided a kind of sorting that molybdenum bismuth is reclaimed in multi-metal sulfide
System, it is characterised in that the separation system includes：Loading hopper, grinding mechanism, Task-size Controlling device, size mixing device, molybdenum bismuth are mixed floating
Mixed float of roughing device, molybdenum bismuth scans device, molybdenum bismuth mixed crude concentrate blank selecting device, the secondary sky of molybdenum bismuth mixed crude concentrate first
White selecting device, molybdenum bismuth bulk concentrate roughing device, that molybdenum bismuth mixed crude concentrate scans device, molybdenum bismuth mixed crude concentrate one-level is selected
Device, molybdenum bismuth mixed crude concentrate two level selecting device, molybdenum bismuth mixed crude concentrate three-level selecting device, molybdenum bismuth mixed crude concentrate level Four
Selecting device；Size mixing device has the water inlet for being used for adjusting pulp density plus lime hole, the first coal oilhole, first plus second
Sulphur nitrogen hole plus Z-200 holes；The mixed floating roughing device of molybdenum bismuth has the slurry inlet connected with size mixing device, to lead to blank selected
First outlet and scan outlet；Molybdenum bismuth is mixed floating to be scanned device and has and scan entrance, with leading to blank essence with scan outlet
The selected second outlet of blank, mine tailing outlet, the second coal oilhole, the second diethyldithiocarbamate hole are led in the first outlet connection of choosing；
Mine tailing exports and mine tailing reservoir；Blank selecting device has first selected with leading to blank to molybdenum bismuth mixed crude concentrate first
The selected first entrance of blank first of outlet, the outlet of the slurry connected with slurry inlet feedback, the selected outlet of blank first；
Molybdenum bismuth mixed crude concentrate secondary blank selecting device has and the selected entrance of secondary blank of the selected outlet of blank first, two
The secondary slurry that the selected outlet of secondary blank, the first outlet selected with leading to blank connects, which feeds back, to be exported；Molybdenum bismuth bulk concentrate is thick
Screening device have exported with the molybdenum bismuth bulk concentrate roughing entrance of the selected outlet of secondary blank, the roughing of molybdenum bismuth bulk concentrate,
Molybdenum bismuth bulk concentrate scans feedback entrance, the first vulcanized sodium added holes, molybdenum bismuth bulk concentrate roughing outlet；Molybdenum bismuth mixed crude concentrate
Device is scanned with the molybdenum bismuth bulk concentrate with molybdenum bismuth bulk concentrate roughing outlet scans entrance, molybdenum bismuth bulk concentrate is scanned
Feedback outlet is scanned in outlet, the molybdenum bismuth bulk concentrate connected with molybdenum bismuth bulk concentrate roughing entrance, and molybdenum bismuth bulk concentrate is scanned out
Mouth connects with bismuth concentrate product container；Molybdenum bismuth mixed crude concentrate one-level selecting device, which has to export with the roughing of molybdenum bismuth bulk concentrate, to be connected
The selected outlet of the selected entrance of logical one-level, one-level, scan with molybdenum bismuth bulk concentrate and to feed back the molybdenum bismuth bulk concentrate that connects of entrance and sweep
The outlet of choosing feedback, the second vulcanized sodium added holes；Molybdenum bismuth mixed crude concentrate two level selecting device has and the selected outlet of one-level
The selected entrance of two level, the selected outlet of two level, the two level feedback that connect with one-level selected entrance exports, the trisulfides sodium adds
Hole；Molybdenum bismuth mixed crude concentrate three-level selecting device has to be chosen with the selected entrance of three-level of the selected outlet of two level, three-level
Mouth, the outlet of the three-level connected with the selected entrance of two level feedback, sodium tetrasulfide added holes；The selected dress of molybdenum bismuth mixed crude concentrate level Four
Put with the selected entrance of level Four with the selected outlet of three-level, the selected outlet of level Four, the level Four connected with the selected entrance of three-level
Feedback outlet, sodium pentosulfide added holes.Sodium pentosulfide added holes connects with molybdenum concntrate product container.
Preferably, loading hopper is in inverted tetragonous cone table shape, the left and right sides of its upper end be provided with two can with automatic turning,
Automatically reset lid, this is covered with rotating shaft and counterweight；The lower end of loading hopper is provided with charging and exported.
Preferably, the grinding mechanism is rod mill.
Preferably, the grinding mechanism is provided with charging import and particle outlet, charging outlet and charging inlet communication.
Preferably, the Task-size Controlling device include particle entrance, I shapes control valve, control spring, particle feedback outlet,
Screen cloth lid, screen cloth lid rotating shaft；I shapes control valve is provided with upper stifled and lower stifled, and lower stifled center and the contact point of control spring are higher than it
Surrounding；Control spring has to be connected by the particle that the screen cloth of upper stifled support covers by the outlet of particle feedback with feeding back to grinding mechanism
Logical the first operating position and it is lower it is stifled because compression occurs for control spring and to block up with the disengaging of screen cloth lid and particle it is anti-
Feed out mouth and feed back to the second operating position that the connection of grinding mechanism is cut off.
In the prior art, the separation operation of molybdenum bismuth is reclaimed in multi-metal sulfide needs a series of equipment, not only sets
Back-up dissipates, floor space is big, and the process needed is more, and the manual operations such as blanking, transport, feeding are needed between process, works
Environment is poor, and pollution is unavoidable, and equipment cost and human cost are all high, but operating efficiency is very low, and therefore, production cost is high,
Deficiency in economic performance, environmental protection are difficult to up to standard.
The utility model overcomes the prejudice of conventional art, creatively develops one kind and is reclaimed in multi-metal sulfide
The separation system of molybdenum bismuth, it is integrated, integration apparatus, and floor space is small, and an equipment, which allows for raw material, to be entered product and go out, no
Multiple operation is needed again, and working environment is good, and efficient production is just realized in one man operation, and therefore, production cost is low, good in economic efficiency, ring
Possess guarantee.
Moreover, implementing the utility model, without using cyanide inhibitor, production pollution is avoided.
Brief description of the drawings
Fig. 1 is the structure principle chart according to the separation system of the present utility model that molybdenum bismuth is reclaimed in multi-metal sulfide；
Fig. 2 is according to the separation operation schematic flow sheet of the present utility model that molybdenum bismuth is reclaimed in multi-metal sulfide.
Embodiment
As shown in figure 1, included according to the separation system 200 of the present utility model that molybdenum bismuth is reclaimed in multi-metal sulfide：
The mixed floating roughing device 50 of loading hopper 10, grinding mechanism 20, Task-size Controlling device 30, size mixing device 40, molybdenum bismuth, mixed float of molybdenum bismuth are scanned
Device 60, molybdenum bismuth mixed crude concentrate blank selecting device 70, molybdenum bismuth mixed crude concentrate secondary blank selecting device 80, molybdenum bismuth first
Bulk concentrate roughing device 90, molybdenum bismuth mixed crude concentrate scan device 100, molybdenum bismuth mixed crude concentrate one-level selecting device 110, molybdenum
Bismuth mixed crude concentrate two level selecting device 120, molybdenum bismuth mixed crude concentrate three-level selecting device 130, molybdenum bismuth mixed crude concentrate level Four
Selecting device 140.
Loading hopper 10 is in inverted tetragonous cone table shape, and the left and right sides of its upper end is provided with two can be with automatic turning, automatic
The lid 11 of reset, spread with reducing the dust after feeding, lid 11 is provided with rotating shaft 12 and counterweight 13.The lower end of loading hopper 10 is set
There is charging outlet 14.
Grinding mechanism 20 can be rod mill；Grinding mechanism 20 is provided with charging import 21 and particle outlet 22.Charging outlet
14 connect with charging import 21.
Task-size Controlling device 30 includes particle entrance 31, I shapes control valve 32, control spring 37, particle feedback outlet 38, sieve
Square 36, screen cloth lid rotating shaft 35, I shapes control valve 32 are provided with upper stifled 33 and lower stifled 34, and lower stifled 34 centre connects with control spring 37
Contact is higher than its surrounding, and the rigidity Design principle of control spring 37 is：It is milled in multi-metal sulfide because particle diameter is less than
0.076mm and fall compression just occurs when the particle on lower stifled 34 accounts for 40 weight % through screen cloth lid 36, so as to be in the
Two operating positions, i.e.,：Block up 34 down to be opened, particle leaks down from lower stifled 34 surrounding；And before this, in the first working position
Put, i.e.,：The screen cloth lid 36 of both sides is all ridden on stifled 33, and particle of the particle diameter more than or equal to 0.076mm cannot pass through screen cloth lid 36
And fall, but grinding mechanism 20 is fed back to by particle feedback outlet 38.
Size mixing device 40 has the water inlet 41 for causing pulp density to be 25~30% plus lime hole 42, the first coal oil
Hole 43, first plus diethyldithiocarbamate hole 44 plus Z-200 holes 45.
The mixed floating roughing device 50 of molybdenum bismuth have the slurry inlet 51 connected with size mixing device 40, lead to blank it is selected first
Export 52 and scan outlet 53.
Molybdenum bismuth is mixed floating scan device 60 have with scan that outlet 53 connect scan entrance 61 and lead to blank it is selected the
One outlet 52 connection lead to the selected second outlet 62 of blank, mine tailing outlet 63, mine tailing container 66, the second coal oilhole 64,
Second diethyldithiocarbamate hole 65.
Blank selecting device 70 has what the first outlet 52 selected with leading to blank connected to molybdenum bismuth mixed crude concentrate first
The selected first entrance 71 of blank, the slurry feedback outlet 73 connected with slurry inlet 51, the selected outlet 72 of blank first first.
Molybdenum bismuth mixed crude concentrate secondary blank selecting device 80 has the secondary sky connected with the selected outlet 72 of blank first
The secondary slurry feedback that the selected outlet 82 of Bai Jingxuan entrances 81, secondary blank, the first outlet 52 selected with leading to blank connect
Outlet 83.
Molybdenum bismuth bulk concentrate roughing device 90 has the molybdenum bismuth bulk concentrate roughing connected with the selected outlet 82 of secondary blank
Entrance 91, the roughing of molybdenum bismuth bulk concentrate outlet 92, molybdenum bismuth bulk concentrate scan feedback entrance 93, the first vulcanized sodium added holes 94,
Molybdenum bismuth bulk concentrate roughing outlet 95.
Molybdenum bismuth mixed crude concentrate scans device 100, and there is the molybdenum bismuth connected with molybdenum bismuth bulk concentrate roughing outlet 95 to mix essence
The molybdenum bismuth mixing that ore deposit scans entrance 101, molybdenum bismuth bulk concentrate scans outlet 102, is connected with molybdenum bismuth bulk concentrate roughing entrance 91
Concentrate scans feedback outlet 103, and molybdenum bismuth bulk concentrate is scanned outlet 102 and connected with bismuth concentrate product container 104.
Molybdenum bismuth mixed crude concentrate one-level selecting device 110 has the one-level essence connected with molybdenum bismuth bulk concentrate roughing outlet 92
The selected outlet 112 of mouth 111, one-level is selected into, is scanned with molybdenum bismuth bulk concentrate and is fed back the molybdenum bismuth bulk concentrate that connects of entrance 93 and scan
The 113, second vulcanized sodium added holes 114 of feedback outlet.
Molybdenum bismuth mixed crude concentrate two level selecting device 120 has the selected entrance of two level connected with the selected outlet 112 of one-level
121st, the two level feedback that the selected outlet 122 of two level, entrance selected with one-level 111 connect exports 123, trisulfides sodium added holes
124。
Molybdenum bismuth mixed crude concentrate three-level selecting device 130 has the selected entrance of three-level connected with the selected outlet 122 of two level
131st, the three-level feedback that the selected outlet 132 of three-level, entrance selected with two level 121 connect exports 133, sodium tetrasulfide added holes
134。
Molybdenum bismuth mixed crude concentrate level Four selecting device 140 has the selected entrance of level Four connected with the selected outlet 132 of three-level
141st, the level Four feedback that the selected outlet 142 of level Four, entrance selected with three-level 131 connect exports 143, sodium pentosulfide added holes
144.Sodium pentosulfide added holes 144 connects with molybdenum concntrate product container 145.
As shown in Fig. 2 the separating technology of the utility model one embodiment comprises at least, using rod mill by more metal sulphur
Change ore deposit is milled to -0.076mm and accounts for 40%, under the conditions of pulp density is 25~30%, adds lime, kerosene, diethyldithiocarbamate, Z-200,
The mixed floating roughing of molybdenum bismuth is carried out after sizing mixing, mine tailing adds kerosene, diethyldithiocarbamate is sized mixing, and carries out molybdenum bismuth afterwards and mixes floating scan.Roughing and
It is selected through blank twice to scan the molybdenum bismuth mixed crude concentrate of acquisition, then, adds vulcanized sodium and sizes mixing, afterwards using it is one thick, sweep,
Four progress greatly the floating molybdenum suppression bismuth of row, and selected operation adds vulcanized sodium and suppresses bismuth mineral, final to obtain molybdenum concntrate and bismuth concentrate.This practicality is new
Type is applied to the multi-metal sulfide that non-target minreal is mainly pyrite.
According to the utility model, multi-metal sulfide is milled to -0.076mm and accounts for 40%, add lime adjustment slurry pH,
Be suppressed the non-target minreal based on pyrite i.e. hydrophilic, then, add target minreal collecting agent kerosene, diethyldithiocarbamate,
Z-200, adsorb makes its hydrophobic on target minreal surface.
Example：
It is respectively 7%, 8% that certain, which selects factory's multi-metal sulfide raw ore grade containing Mo, Bi, and it is inhibitor to it to use cyanide
Multi-metal sulfide is reclaimed, and obtains molybdenum concntrate ＞ containing Mo 50%, Mo rate of recovery ＞ 85%, bismuth concentrate ＞ containing Bi 25%, Bi
Rate of recovery ＞ 50%.
Scene uses regime of agent of the present utility model, only changes roughing flotation concentration, does not change original technological process, i.e.,
Concentrate ＞ containing Mo 50%, Mo rate of recovery ＞ 90%, bismuth concentrate ＞ containing Bi 30%, Bi rate of recovery ＞ 75% can be obtained.
According to the utility model, after multi-metal sulfide is milled into target minreal monomer dissociation, adds specific medicament and adjust
The pH value of whole ore pulp.Inhibitor is firstly added, is suppressed non-target minreal i.e. hydrophilic.Then, appropriate purpose ore deposit is added
Thing collecting agent, adsorb makes its hydrophobic on target minreal surface.Foaming agent is eventually adding, is made containing on hydrophobic target minreal
It is floating.
Experiment proves, implements the utility model, can equally obtain the flotation in the prior art using cyanide as inhibitor and refer to
Mark, but fundamentally solves production pollution problem.
Claims (5)
1. the separation system of molybdenum bismuth is reclaimed in multi-metal sulfide, it is characterised in that the separation system includes：Loading hopper, mill
The mixed floating roughing device of crushing device, Task-size Controlling device, size mixing device, molybdenum bismuth, mixed float of molybdenum bismuth scan device, molybdenum bismuth mixed crude concentrate
Blank selecting device, molybdenum bismuth mixed crude concentrate secondary blank selecting device, molybdenum bismuth bulk concentrate roughing device, the mixing of molybdenum bismuth first
Rough concentrate scans device, molybdenum bismuth mixed crude concentrate one-level selecting device, molybdenum bismuth mixed crude concentrate two level selecting device, the mixing of molybdenum bismuth
Rough concentrate three-level selecting device, molybdenum bismuth mixed crude concentrate level Four selecting device；Size mixing device, which has, to be used to adjust pulp density
Water inlet plus lime hole, the first coal oilhole, first plus diethyldithiocarbamate hole plus Z-200 holes；The mixed floating roughing device of molybdenum bismuth have with
The slurry inlet of size mixing device connection, lead to the selected first outlet of blank and scan outlet；Molybdenum bismuth is mixed floating, which to scan device, has
With scan outlet scan entrance, the first outlet selected with leading to blank connects leads to that blank is selected second to be gone out
Mouth, mine tailing outlet, the second coal oilhole, the second diethyldithiocarbamate hole；Mine tailing exports and mine tailing reservoir；Molybdenum bismuth mixed crude concentrate is first
Secondary blank selecting device has the selected first entrance of blank first that the first outlet selected with leading to blank connect, entered with slurry
The outlet of slurry feedback, the selected outlet of blank first of mouth connection；Molybdenum bismuth mixed crude concentrate secondary blank selecting device has and head
The selected outlet of the selected entrance of secondary blank of the secondary selected outlet of blank, secondary blank, with leading to that blank is selected first to be gone out
The secondary slurry feedback outlet of mouth connection；Molybdenum bismuth bulk concentrate roughing device has the molybdenum bismuth with the selected outlet of secondary blank
Bulk concentrate roughing entrance, molybdenum bismuth bulk concentrate roughing outlet, molybdenum bismuth bulk concentrate scan feedback entrance, the addition of the first vulcanized sodium
Hole, molybdenum bismuth bulk concentrate roughing outlet；Molybdenum bismuth mixed crude concentrate, which scans device, to be had and molybdenum bismuth bulk concentrate roughing outlet
Molybdenum bismuth bulk concentrate scan entrance, molybdenum bismuth bulk concentrate scans outlet, the molybdenum bismuth that is connected with molybdenum bismuth bulk concentrate roughing entrance
Bulk concentrate scans feedback outlet, and molybdenum bismuth bulk concentrate is scanned outlet and connected with bismuth concentrate product container；Molybdenum bismuth mixed crude concentrate
One-level selecting device has and the selected entrance of one-level of molybdenum bismuth bulk concentrate roughing outlet, the selected outlet of one-level and molybdenum bismuth
The molybdenum bismuth bulk concentrate that bulk concentrate scans feedback entrance connection scans feedback outlet, the second vulcanized sodium added holes；Molybdenum bismuth mixes
Rough concentrate two level selecting device has and the selected entrance of two level of the selected outlet of one-level, the selected outlet of two level and one-level essence
It is selected into the two level feedback outlet of mouth connection, trisulfides sodium added holes；Molybdenum bismuth mixed crude concentrate three-level selecting device has and two
The selected outlet of the selected entrance of three-level of the selected outlet of level, three-level, three-level connect with two level selected entrance feed back export, the
Sodium tetrasulfide added holes；Molybdenum bismuth mixed crude concentrate level Four selecting device have with the level Four of the selected outlet of three-level it is selected enter
The selected outlet of mouth, level Four, the level Four feedback outlet connected with the selected entrance of three-level, sodium pentosulfide added holes；Sodium pentosulfide
Added holes connects with molybdenum concntrate product container.
2. the separation system of molybdenum bismuth is reclaimed in multi-metal sulfide as claimed in claim 1, it is characterised in that loading hopper is in
Inverted tetragonous cone table shape, the left and right sides of its upper end is provided with two can be with automatic turning, automatically reset lid, and this, which is covered with, turns
Axle and counterweight；The lower end of loading hopper is provided with charging and exported.
3. the separation system of molybdenum bismuth is reclaimed in multi-metal sulfide as claimed in claim 1, it is characterised in that described to grind
Device is rod mill.
4. the separation system of molybdenum bismuth is reclaimed in multi-metal sulfide as claimed in claim 1, it is characterised in that described to grind
Device is provided with charging import and particle outlet, charging outlet and charging inlet communication.
5. the separation system of molybdenum bismuth is reclaimed in multi-metal sulfide as claimed in claim 1, it is characterised in that the granularity
Control device includes particle entrance, I shapes control valve, control spring, the outlet of particle feedback, screen cloth lid, screen cloth lid rotating shaft；I shape controls
Valve processed is provided with upper stifled and lower stifled, and lower stifled center and the contact point of control spring are higher than its surrounding；Spring is controlled to have by upper stifled
The particle that the screen cloth of support covers is by the outlet of particle feedback with feeding back to the first operating position that grinding mechanism connects and lower blocking up
Because compression occurs for control spring and make it that stifled and screen cloth lid departs from and the outlet of particle feedback is with feeding back to grinding mechanism
Cut-off the second operating position of connection.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720296185.4U CN207086120U (en) | 2017-03-24 | 2017-03-24 | The separation system of molybdenum bismuth is reclaimed in multi-metal sulfide |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720296185.4U CN207086120U (en) | 2017-03-24 | 2017-03-24 | The separation system of molybdenum bismuth is reclaimed in multi-metal sulfide |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112337656A (en) * | 2020-10-15 | 2021-02-09 | 湖南柿竹园有色金属有限责任公司 | Method for improving molybdenum-bismuth-sulfur beneficiation index and wastewater recycling |
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2017
- 2017-03-24 CN CN201720296185.4U patent/CN207086120U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112337656A (en) * | 2020-10-15 | 2021-02-09 | 湖南柿竹园有色金属有限责任公司 | Method for improving molybdenum-bismuth-sulfur beneficiation index and wastewater recycling |
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