CN205761642U - Silicon ash ore reduction separation system - Google Patents

Silicon ash ore reduction separation system Download PDF

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Publication number
CN205761642U
CN205761642U CN201620704586.4U CN201620704586U CN205761642U CN 205761642 U CN205761642 U CN 205761642U CN 201620704586 U CN201620704586 U CN 201620704586U CN 205761642 U CN205761642 U CN 205761642U
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CN
China
Prior art keywords
vibrosieve
connects
conveyer
elevator
silicon ash
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201620704586.4U
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Chinese (zh)
Inventor
牟舟
牟一舟
牟亚东
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lianzhou Xinyu Mineral Products Co Ltd
Original Assignee
Lianzhou Xinyu Mineral Products Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Lianzhou Xinyu Mineral Products Co Ltd filed Critical Lianzhou Xinyu Mineral Products Co Ltd
Priority to CN201620704586.4U priority Critical patent/CN205761642U/en
Application granted granted Critical
Publication of CN205761642U publication Critical patent/CN205761642U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model discloses a kind of silicon ash ore reduction separation system, including jaw crusher, vibrosieve, elevator and whirlwind disintegrating machine, described jaw crusher exit connects described vibrosieve by pipeline, described vibrosieve is provided with inside top discharge mouth and lower discharge port and described vibrosieve and is provided with screen cloth and is positioned at the first conveyer device below screen cloth, described screen cloth correspondence connects described top discharge mouth, described first conveyer device correspondence connects described lower discharge port, the second conveyer device is set at described top discharge mouth, the 3rd transporter is set at described lower discharge port, described second conveyer device connects described elevator, elevator upper end connects described whirlwind disintegrating machine.This utility model belongs to ore sizing processing technique field, by optimizing the operation of wollastonite mine sorting, reduce follow-up broken, separate the design requirement to equipment in producing, saved cost of equipment maintenance.

Description

Silicon ash ore reduction separation system
Technical field
This utility model relates to Ore sorting processing technique field, is specifically related to a kind of wollastonite mine crushing-separating apparatus.
Background technology
Wollastonite is widely used in the industries such as pottery, metallurgy, building, machinery, electronics and papermaking, as rubber, plastics, tree The filler of fat, paint, coating etc., gas filtering material, heat-barrier material or flux etc..
Wollastonite mine is the nonmetallic minerals of a kind of metasilicate, and mainly originate in Intermediate-acid Intrusive and limestone contacts change Matter band, mineral mostly are wollastonite, and association product has quartz, calcite etc..Ore dressing mode commonly uses picking, magnetic separation, flotation and color choosing.
Beneficiation method commonly used by wollastonite has, and in unit for inertial conic pulverizer or autogenous tumbling mill, ore deposit is carried out dry type pulverizing and air 1.0mm and 0.071mm classification is pressed in finishing, and grade is that the carrying out of+1.0mm is pulverized again, and grade is the conduct of-0.071mm Final wollastonite product, grade be-1.0+0.071mm carry out magnetic separation, obtain garnet concentrate.Extracting wollastonite Before concentrate, non-magnetic product experience triboelectrification, electric tube furnace is heated to 150-170 DEG C, then at oscillating feeder It is cooled to 100-110 DEG C on dish, sets electric field density as 3.5*105-3.9*105V/m, extracts wollastonite by electrostatic separation Concentrate and simultaneously extraction calcite concentrate and quartz products.The method is complex, and processing conditions is harsh, and commercial application becomes This height.
The patent of publication number CN101003026A discloses a kind of grinder for needle tabular spar, and jaw crusher is by promoting Machine and pipeline are connected with making hammer pulverizer, and the discharging opening making hammer pulverizer is connected with sucking spiral multiple-stage separator by pipeline Connect, spiral multiple-stage separator be provided above air-introduced machine.This invention achieves the multiple stage separation of Ore, improves work effect Rate.But adding and beat hammer disintegrating machine and the burden of multiple-stage separator, the product design of air exercise hammer disintegrating machine and multiple-stage separator is wanted Ask higher, not so can not meet separation requirement.
Utility model content
The utility model discloses a kind of silicon ash ore reduction separation system, it is intended to reduce broken in Ore production process and The burden of separation equipment, optimizes separable programming to improve product quality.
Silicon ash ore reduction separation system, including jaw crusher, vibrosieve, elevator and whirlwind disintegrating machine, described Hubei Province Formula disintegrating machine exit connects described vibrosieve by pipeline, described vibrosieve be provided with top discharge mouth and lower discharge port and described in shake Dynamic sieve is internal to be provided with screen cloth and is positioned at the first conveyer device below screen cloth, and described screen cloth correspondence connects described top discharge mouth, institute State the first conveyer device correspondence and connect described lower discharge port, at described top discharge mouth, set the second conveyer device, described lower discharge port Place sets the 3rd transporter, and described second conveyer device connects described elevator, and elevator upper end connects described whirlwind disintegrating machine. More excellent, it is provided with skewed slot in the middle of the tail end at described dark pavilion.
More excellent, described whirlwind disintegrating machine is connected by dust outlet tube dust settling pocket.
More excellent, described screen slope is arranged.
More excellent, described vibrosieve is ore classification vibrosieve.
A kind of silicon ash ore reduction separation system that this utility model provides, Ore i.e. carries out after tentatively pulverizing sieving for the first time Choosing, reduce follow-up broken, separate the design requirement to equipment in producing, saved cost of equipment maintenance.
Accompanying drawing explanation
In order to be illustrated more clearly that this utility model embodiment or technical scheme of the prior art, below will be to embodiment Or the required accompanying drawing used is briefly described in description of the prior art, it should be apparent that, the accompanying drawing in describing below is only It is embodiments more of the present utility model, for those of ordinary skill in the art, in the premise not paying creative work Under, it is also possible to other accompanying drawing is obtained according to these accompanying drawings.
Fig. 1 is principle schematic of the present utility model.
Detailed description of the invention
A kind of silicon ash ore reduction separation system that the utility model discloses, excellent by Ore being sorted the design of operation Change, reduce follow-up broken, separate the design requirement to equipment in producing, saved cost of equipment maintenance.
Below in conjunction with the accompanying drawing in this utility model, the technical scheme in this utility model is carried out clearly and completely Describe, it is clear that described is only a part of embodiment of this utility model rather than whole embodiments.Based on this practicality Embodiment in novel, it is every other that those of ordinary skill in the art are obtained on the premise of not making creative work Embodiment, broadly falls into the scope of this utility model protection.
As it is shown in figure 1, include jaw crusher 1, vibrosieve 3, elevator 8 and whirlwind disintegrating machine 9, described jaw crusher 1 exit connects described vibrosieve 3 by pipeline 2, and described vibrosieve 3 is provided with top discharge mouth and lower discharge port and described vibrosieve 3 inside are provided with screen cloth 7 and are positioned at the first conveyer device 4 below screen cloth 7, and described screen cloth 7 is corresponding connects described top discharge mouth, institute State the first conveyer device 4 described lower discharge port of corresponding connection, at described top discharge mouth, set the second conveyer device 6, described bottom discharge Setting the 3rd transporter 5 at Kou, described second conveyer device 6 connects described elevator 8, and elevator 8 upper end connects described whirlwind Disintegrating machine 9.
Preferably, described vibrosieve 3 is ore classification vibrosieve, and described screen cloth 7 is obliquely installed, and is provided with angle and adjusts Regulating device, range of accommodation is 8 °~25 °, and described whirlwind disintegrating machine upper end is connected by dust outlet tube 11 dust settling pocket 10.
Operation principle of the present utility model:
Wollastonite mine enters vibrosieve 3 after jaw crusher 1 is tentatively pulverized, and after preliminary pulverizing, the Ore of bulk is sent to Second conveyer device 6, the powder body after preliminary pulverizing is sent to the 3rd conveyer device 5 and carries out subsequent treatment, at the second conveyer device 6 On by the bulk silicon lime stone of picking separation high-quality, remaining Ore is sent to whirlwind disintegrating machine 9 after entering elevator 8 and carries out secondary Broken, the dust produced after whirlwind disintegrating machine 9 is broken enters dust settling pocket to reduce dust recycling.
Wollastonite mine carries out classification after primary comminution, and color selects the wollastonite of high-quality, removes the wollastonite sheet of low content, The Ore that remaining ore particles is bigger enters in whirlwind disintegrating machine pulverize with the second conveyer device, elevator, and granule is less Ore is ground pulverizing.
By above description, silicon ash ore reduction separation system disclosed in this utility model, tentatively pulverize at Ore After, it is processed after Ore being sorted by classifying screen, the wollastonite mine of available different qualities, decreases garnet, Fang Xie Stone etc. are mixed into the content of high quality silicon lime stone, and different grades of wollastonite mine can break up process, provide convenient to the screening of Ore later stage.
Above content is to combine concrete preferred implementation further detailed description of the utility model, it is impossible to Assert that of the present utility model being embodied as is confined to these explanations.Ordinary skill for this utility model art For personnel, without departing from the concept of the premise utility, it is also possible to make some simple deduction or replace, all should regard For belonging to protection domain of the present utility model.

Claims (4)

1. silicon ash ore reduction separation system, including jaw crusher, vibrosieve, elevator and whirlwind disintegrating machine, its feature exists In, described jaw crusher exit connects described vibrosieve by pipeline, and described vibrosieve is provided with top discharge mouth and bottom discharge Being provided with screen cloth inside mouth and described vibrosieve and be positioned at the first conveyer device below screen cloth, described screen cloth correspondence connects on described Discharging opening, described first conveyer device correspondence connects described lower discharge port, sets the second conveyer device at described top discharge mouth, described Setting the 3rd transporter at lower discharge port, described second conveyer device connects described elevator, and elevator upper end connects described rotation Wind disintegrating machine.
Silicon ash ore reduction separation system the most according to claim 1, it is characterised in that described whirlwind disintegrating machine passes through Dirt pipe connects dust settling pocket.
Silicon ash ore reduction separation system the most according to claim 1, it is characterised in that described screen slope is arranged.
Silicon ash ore reduction separation system the most according to claim 1, it is characterised in that described vibrosieve is ore classification Vibrosieve.
CN201620704586.4U 2016-07-06 2016-07-06 Silicon ash ore reduction separation system Expired - Fee Related CN205761642U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620704586.4U CN205761642U (en) 2016-07-06 2016-07-06 Silicon ash ore reduction separation system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620704586.4U CN205761642U (en) 2016-07-06 2016-07-06 Silicon ash ore reduction separation system

Publications (1)

Publication Number Publication Date
CN205761642U true CN205761642U (en) 2016-12-07

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Application Number Title Priority Date Filing Date
CN201620704586.4U Expired - Fee Related CN205761642U (en) 2016-07-06 2016-07-06 Silicon ash ore reduction separation system

Country Status (1)

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CN (1) CN205761642U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107413495A (en) * 2017-07-14 2017-12-01 望江县金峰矿产品科技有限公司 A kind of silica multi-stage crushing screening machine
CN111843811A (en) * 2020-08-05 2020-10-30 卢昌敏 Silica processing preprocessing device
CN112076870A (en) * 2020-09-06 2020-12-15 陈丽萍 Copper extraction and deironing equipment for copper ore acid leaching solution

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107413495A (en) * 2017-07-14 2017-12-01 望江县金峰矿产品科技有限公司 A kind of silica multi-stage crushing screening machine
CN111843811A (en) * 2020-08-05 2020-10-30 卢昌敏 Silica processing preprocessing device
CN112076870A (en) * 2020-09-06 2020-12-15 陈丽萍 Copper extraction and deironing equipment for copper ore acid leaching solution

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C14 Grant of patent or utility model
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20161207

Termination date: 20200706

CF01 Termination of patent right due to non-payment of annual fee