CN201702015U - Novel gold concentration device - Google Patents
Novel gold concentration device Download PDFInfo
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- CN201702015U CN201702015U CN2010202526413U CN201020252641U CN201702015U CN 201702015 U CN201702015 U CN 201702015U CN 2010202526413 U CN2010202526413 U CN 2010202526413U CN 201020252641 U CN201020252641 U CN 201020252641U CN 201702015 U CN201702015 U CN 201702015U
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Abstract
The utility model belongs to the technical field of gold concentration, and particularly relates to a novel gold concentration device. Raw ores are crushed via a high-efficient high-pressure roller mill, crushed products are classified by means of screening, final products generated after screening are milled via a ball mill and a classification mechanism which form a closed loop, differential floatation is performed on the classified overflowing products, rough floatation concentrates are cleaned by three times to generate final concentrates, and rough tailings are scavenged twice to obtain final tail floatation concentrates to perform roughing floatation and recycle. Compared with the prior art, by adopting the high-pressure roller mill, the novel gold concentration device has the advantages of high crushing efficiency, high fine fraction content in final crushed products and strong crushing ability. The fine fraction content of the final crushed products is high so as to lower ore milling energy consumption, and predicated comprehensive energy consumption of crushing and milling operation of the high-pressure roller mill can be reduced by 20% to 30%.
Description
Technical field
The utility model belongs to the gold ore equipment technical field, particularly a kind of gold ore new equipment.
Background technology
Present dressing process for gold ore is two section one a closed circuit crushing technology, one section one closed circuit grinding technology, flotation is an one roughing, triple cleaning, secondary are swept flotation and the technological process of flotation chats for returning in proper order, and this technological process is the old process that gold ore adopted, this kind technological process crushing efficiency is low, the break process ability is low, and is longer during the breaker, and the fine fraction product content is low in the crushed product.This directly has influence on the raising of follow-up grinding flotation disposal ability, and sorting result is bad.Application for a patent for invention 00123984.8<a kind of dressing process for gold ore〉employing two and half one closed circuit crushings, two section two closed circuit grinding is then again through diffeential floatation, selected, its mine tailing through one slightly sweep the other operation of flotation after, with cleaner tailings with sweep flotation concentrate and concentrate in together and merge the raw ore regrinding and reconcentration, this kind technology and other dressing process for gold ore adopt two section one closed circuit crushing, two section two closed circuit crushing, the crushing circuit complexity, particle size after cracking is thicker, be unfavorable for follow-up grinding operation, the device processes amount is low, equipment investment volume height.
Summary of the invention
The purpose of this utility model is the deficiency that overcomes original technology, provides a kind of flow process simple, crushing efficiency height, the gold ore new equipment that energy consumption and cost are low.
The purpose of this utility model realizes by following technical proposals:
Gold ore new equipment of the present utility model, it is characterized in that by feed hopper, the feed hopper belt conveyer that continues mutually therewith, the consecutive disintegrating machine of belt conveyer therewith, the consecutive screening machine of disintegrating machine therewith, the consecutive ball mill of screening machine therewith, the consecutive cyclone of ball mill therewith, the consecutive rough floatation machine of cyclone therewith, difference is the consecutive cleaner flotation machine of rough floatation machine therewith, once sweep flotation device, the consecutive secondary cleaner flotation of cleaner flotation machine machine therewith, consecutive three cleaner flotation machines of secondary cleaner flotation machine therewith, once sweep the consecutive secondary of flotation device therewith and sweep flotation device and form, a described cleaner flotation machine also continues mutually with the described flotation device of once sweeping.
Described disintegrating machine is a high-pressure roller mill.
Described ball mill is a grate ball mill, and described screening machine is a vibratory sieve.
Adopt the ore-dressing technique of gold ore new equipment of the present utility model to comprise the steps:
1) raw ore that enters feed hopper is sent into disintegrating machine by belt conveyer and is carried out fragmentation,
2) crushed product of disintegrating machine is sent into screening machine and sieve, the oversize of screening machine returns disintegrating machine and continues fragmentation, and the undersize of screening machine is sent into the ball mill ore grinding,
3) ball mill and screening machine constitute closed-circuit system, and the ore milling product of ball mill enters cyclone classification, and the cyclone overflow is sent into the rough floatation machine and roughly selected, and the sediment of cyclone returns ball mill and continues ore grinding,
4) concentrate of roughly selecting of rough floatation machine is sent into the first cleaner flotation machine and is carried out selected, the mine tailing of the first cleaner flotation machine is sent into and is for the first time swept flotation device and carry out sweeping the first time flotation, sweeping for the first time flotation concentrate returns the rough floatation machine and continues to sort, the secondary cleaner flotation is carried out in the concentrate of cleaner flotation machine inflow for the first time cleaner flotation machine for the second time
5) mine tailing of secondary cleaner flotation machine returns the cleaner flotation machine one time, and the concentrate that secondary cleaner flotation machine is selected is sent into three cleaner flotation machines and continued to sort, and the mine tailing of three cleaner flotation machines returns secondary cleaner flotation machine, and three times the resulting concentrate of cleaner flotation machine is exactly a final concentrate,
6) once sweep mine tailing that flotation obtains and enter secondary and sweep flotation device and carry out secondary and sweep flotation, the mine tailing that secondary is swept flotation is a true tailings, and secondary is swept flotation concentrate and returned and once sweep flotation.
Gold ore new equipment of the present utility model, raw ore is by the fragmentation of efficient high-pressure roller mill, crushed product passes through sieve classification, final products after the screening constitute closed circuit grinding by the ball mill ore grinding and with grader, classification overflow product carries out diffeential floatation, the rough floatation concentrate carries out selected formation final concentrate 3 times, and rougher tailings carries out sweeping for twice flotation and obtains finality, sweeps flotation concentrate and returns to roughly select and circulate.
The utility model has following good effect compared with the prior art: because the utility model adopts high-pressure roller mill whole crushing circuit of generation, the device processes amount is big, and flow process is simple, the crushing efficiency height, broken final products fine fraction content height, break process ability height.Broken final products fine fraction content height causes power consume to reduce.Can make the comprehensive energy consumption of broken and grinding operation save 20%~30%.
Description of drawings
Fig. 1 is an apparatus structure block diagram of the present utility model.
The specific embodiment
Describe the specific embodiment of the present utility model in detail below in conjunction with accompanying drawing.
As shown in Figure 1, gold ore new equipment of the present utility model, it is characterized in that by feed hopper, the feed hopper belt conveyer that continues mutually therewith, the consecutive disintegrating machine of belt conveyer therewith, the consecutive screening machine of disintegrating machine therewith, the consecutive ball mill of screening machine therewith, the consecutive cyclone of ball mill therewith, the consecutive rough floatation machine of cyclone therewith, difference is the consecutive cleaner flotation machine of rough floatation machine therewith, once sweep flotation device, the consecutive secondary cleaner flotation of cleaner flotation machine machine therewith, consecutive three cleaner flotation machines of secondary cleaner flotation machine are therewith once swept the consecutive secondary of flotation device therewith and are swept flotation device and form, and a described cleaner flotation machine also continues mutually with the described flotation device of once sweeping.
Described disintegrating machine is a high-pressure roller mill.
Described ball mill is a grate ball mill, and described screening machine is a vibratory sieve.
Gold ore new equipment of the present utility model, raw ore is by the fragmentation of efficient high-pressure roller mill, crushed product passes through sieve classification, final products after the screening constitute closed circuit grinding by the ball mill ore grinding and with classification mechanism, classification overflow product carries out diffeential floatation, the rough floatation concentrate carries out triple cleaning and forms final concentrate, rougher tailings carries out sweeping for twice flotation and obtains finality and sweep flotation concentrate and return to roughly select and circulate, the utility model has following good effect compared with the prior art: because the utility model adopts the high pressure kibbler roll, the crushing efficiency height, broken final products fine fraction content height, break process ability height.Broken final products fine fraction content height causes power consume to reduce.The prediction high-pressure roller mill can make the comprehensive energy consumption of broken and grinding operation save 20%~30%.
Claims (3)
1. gold ore new equipment, it is characterized in that by feed hopper, the feed hopper belt conveyer that continues mutually therewith, the consecutive disintegrating machine of belt conveyer therewith, the consecutive screening machine of disintegrating machine therewith, the consecutive ball mill of screening machine therewith, the consecutive cyclone of ball mill therewith, the consecutive rough floatation machine of cyclone therewith, difference is the consecutive cleaner flotation machine of rough floatation machine therewith, once sweep flotation device, the consecutive secondary cleaner flotation of cleaner flotation machine machine therewith, consecutive three cleaner flotation machines of secondary cleaner flotation machine therewith, once sweep the consecutive secondary of flotation device therewith and sweep flotation device and form, a described cleaner flotation machine also continues mutually with the described flotation device of once sweeping.
2. gold ore new equipment according to claim 1 is characterized in that described disintegrating machine is a high-pressure roller mill.
3. gold ore new equipment according to claim 1 is characterized in that described ball mill is a grate ball mill, and described screening machine is a vibratory sieve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010202526413U CN201702015U (en) | 2010-07-09 | 2010-07-09 | Novel gold concentration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN2010202526413U CN201702015U (en) | 2010-07-09 | 2010-07-09 | Novel gold concentration device |
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CN201702015U true CN201702015U (en) | 2011-01-12 |
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CN2010202526413U Expired - Fee Related CN201702015U (en) | 2010-07-09 | 2010-07-09 | Novel gold concentration device |
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Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102755921A (en) * | 2012-07-13 | 2012-10-31 | 河南东大矿业股份有限公司 | Bauxite ore dressing and dissociation combination equipment |
CN103846137A (en) * | 2012-11-28 | 2014-06-11 | 沈阳铝镁设计研究院有限公司 | Bauxite grinding method |
CN104148167A (en) * | 2014-08-06 | 2014-11-19 | 哈巴河金坝矿业有限公司 | Reselection recovery method and device for gold |
CN108722881A (en) * | 2018-04-24 | 2018-11-02 | 福建金东矿业股份有限公司 | A kind of metal in chamber box settling sand captures beneficiation method |
CN109201286A (en) * | 2018-11-19 | 2019-01-15 | 洛阳栾川钼业集团股份有限公司 | A kind of grind grading method improving molybdenum ore treating capacity |
CN114534907A (en) * | 2022-03-09 | 2022-05-27 | 中国矿业大学 | Enrichment method and system of low-grade gold ore |
CN115254398A (en) * | 2022-09-01 | 2022-11-01 | 山东黄金矿业科技有限公司选冶实验室分公司 | Method for pre-selecting and discarding gold ores and reducing excessive grinding |
-
2010
- 2010-07-09 CN CN2010202526413U patent/CN201702015U/en not_active Expired - Fee Related
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102755921A (en) * | 2012-07-13 | 2012-10-31 | 河南东大矿业股份有限公司 | Bauxite ore dressing and dissociation combination equipment |
CN103846137A (en) * | 2012-11-28 | 2014-06-11 | 沈阳铝镁设计研究院有限公司 | Bauxite grinding method |
CN104148167A (en) * | 2014-08-06 | 2014-11-19 | 哈巴河金坝矿业有限公司 | Reselection recovery method and device for gold |
CN108722881A (en) * | 2018-04-24 | 2018-11-02 | 福建金东矿业股份有限公司 | A kind of metal in chamber box settling sand captures beneficiation method |
CN109201286A (en) * | 2018-11-19 | 2019-01-15 | 洛阳栾川钼业集团股份有限公司 | A kind of grind grading method improving molybdenum ore treating capacity |
CN114534907A (en) * | 2022-03-09 | 2022-05-27 | 中国矿业大学 | Enrichment method and system of low-grade gold ore |
CN115254398A (en) * | 2022-09-01 | 2022-11-01 | 山东黄金矿业科技有限公司选冶实验室分公司 | Method for pre-selecting and discarding gold ores and reducing excessive grinding |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee | ||
CP01 | Change in the name or title of a patent holder |
Address after: 114001 Anshan District, Liaoning, No. 219 Road, No. 39, Tiedong Patentee after: Anshan Iron and Steel Group Mining Co., Ltd. Address before: 114001 Anshan District, Liaoning, No. 219 Road, No. 39, Tiedong Patentee before: Anshan Iron & Steel Group Mining Co., Ltd. |
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CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20110112 Termination date: 20180709 |
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CF01 | Termination of patent right due to non-payment of annual fee |