CN106191458A - A kind of process reclaiming coarse gold in grinding circuit in advance - Google Patents

A kind of process reclaiming coarse gold in grinding circuit in advance Download PDF

Info

Publication number
CN106191458A
CN106191458A CN201610532320.0A CN201610532320A CN106191458A CN 106191458 A CN106191458 A CN 106191458A CN 201610532320 A CN201610532320 A CN 201610532320A CN 106191458 A CN106191458 A CN 106191458A
Authority
CN
China
Prior art keywords
riffler
hydrocyclone
product
advance
grinding
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.)
Pending
Application number
CN201610532320.0A
Other languages
Chinese (zh)
Inventor
张广伟
李泽理
仝丽娟
王琴
谭文才
张旺
李葆生
闫昊天
郑竞
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.)
CITIC Heavy Industries Co Ltd
Original Assignee
CITIC Heavy Industries 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 CITIC Heavy Industries Co Ltd filed Critical CITIC Heavy Industries Co Ltd
Priority to CN201610532320.0A priority Critical patent/CN106191458A/en
Publication of CN106191458A publication Critical patent/CN106191458A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B11/00Obtaining noble metals
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention discloses a kind of process reclaiming coarse gold in grinding circuit in advance, comprise the following steps: first, carry out ore grinding process by feeding ball mill after crushing raw ore, then feed hydrocyclone pump pond and obtain slurry;Secondly, slurry is delivered to hydrocyclone group and carries out staged care, obtain overflow product and underflow product, underflow product is emitted into riffler, riffler includes 1# riffler and 2# riffler, being configured and control the unlatching quantity of hydrocyclone by hydrocyclone mounting structure, can make 2/3 entrance 1# riffler of underflow product population, 1/3 enters 2# riffler;Finally, the underflow product in 2# riffler feeding vibrosieve and carries out sieve classification process, oversize returns to hydrocyclone pump pond, and undersize feeds centrifugal reselection machine and carries out gravity separation, selects coarse gold;The present invention can reduce technological equipment investment, reduces occupation area of equipment, and is effectively improved the response rate of gold.

Description

A kind of process reclaiming coarse gold in grinding circuit in advance
Technical field
The present invention relates to gold mine process field, concretely relate to a kind of in grinding circuit, reclaim coarse gold in advance Process.
Background technology
In rocked-gold mine, though gravity separation technology is not the main gold means that carry, but gravity treatment has and does not consumes medicament, and environment is dirty Contaminating little, device structure is simple, low power consumption and other advantages, thus most of rocked-gold mine is all provided with gravity treatment work in technological process Skill, in order to reclaim monomeric gold.But in current gold gravity separation technology, the technique such as conventional chute, jigging, shaking table and artificial elutriation There is the shortcomings such as treatment effeciency is low, occupation area of equipment is big, not only hand labor intensity is big, and the response rate of gold is relatively low, point Select the low meeting of efficiency to cause the thick gold of part to enter follow-up Carbon-in-leach flow process, and current conventional extraction time cannot be by molten for thick gold Solving, thus cause it to enter mine tailing, indivedual ore dressing plants there will be gold grade in part mine tailing and, close or larger than the situation of raw ore, make Become the serious golden wasting of resources, also can affect the economic benefit of enterprise simultaneously.
Summary of the invention
It is an object of the invention to, provide one to return in advance in grinding circuit for solving problems of the prior art Receive the process of coarse gold, it is possible to decrease technological equipment investment, reduce occupation area of equipment, and be effectively improved the response rate of gold.
For achieving the above object, the technical solution adopted in the present invention is: one reclaims coarse grain in grinding circuit in advance The process of gold, this process comprises the following steps:
Step one, being 0-12mm by crushing raw ore to granularity, crushed product feeds ball mill and carries out ore grinding process, obtains grinding machine row Material, mill discharge feeds hydrocyclone pump pond and obtains slurry;
Step 2, the slurry obtained is delivered to hydrocyclone group by Pulp pump carries out staged care, waterpower in step one The feed pressure of a cluster cyclone is 0.1MPa to 0.18MPa, after the classified process of hydrocyclone group available overflow product and Underflow product, overflow product, after deslagging screen processes, is delivered to concentrate and Cyanide Leaching workshop, and underflow product is emitted into is located at water The riffler of power a cluster cyclone lower end, riffler includes that 1# riffler and 2# riffler, 1# riffler and 2# riffler are respectively provided with For semi-circular flume structure, 1# riffler is connected to ball mill material inlet by a desilting pipeline, and 2# riffler passes through a desilting Pipeline is connected to the vibrosieve material inlet of gravity treatment system, by the configuration of hydrocyclone mounting structure and Valve controlling hydraulic cyclone The unlatching quantity of device, regulation and control underflow product enters vibrosieve and the ratio of ball mill;
Underflow product in step 3,2# riffler feeds vibrosieve and carries out sieve classification process, and oversize returns waterpower rotation Stream device pump pond, through-screen size is-2mm, feeds centrifugal reselection machine and carries out gravity separation, selects coarse gold, through gravity separation After the mine tailing that obtains return to hydrocyclone pump pond.
By the configuration of hydrocyclone mounting structure and the unlatching quantity of Valve controlling hydrocyclone, underflow product can be made 2/3 entrance 1# riffler of total amount, 1/3 entrance 2# riffler of underflow product population.
In 1# riffler and 2# riffler, the ratio of underflow product entrance vibrosieve and ball mill can be according to grinding system Circulating load adjusts, and Adjustment principle is to make the material ratio mine-supplying quantity new with grinding system of entrance gravity treatment system suitable.
Centrifugal reselection machine in step 3 uses 60g gravitational field and fluidised Codium fragile (Sur.) Har. scattered enrichment bed to carry out at sorting Reason.
Crushed product in step one feeds ball mill by belt conveyor and carries out wet milling process.
Mill discharge in step one is from flowing to hydrocyclone pump pond.
Compared with prior art, the invention have the benefit that
1, technological process of the present invention is simple, by transforming traditional hydrocyclone single annular riffler as two dicyclos The transformation of shape flume structure, after graded operation completes, can realize ore pulp and be allocated in the ratio of technological requirement, instead of ore deposit Slurry allotter, can effectively lower equipment setting height(from bottom), simplifies ore pulp pipeline and arranges, optimizes plant layout structure.Consider ball milling In machine-cyclone closed circuit grinding, ore pulp circulation ratio is high, and system circulating load generally up to 250 ~ 350%, adds in cycle operation Entering when sorting in advance, can cause material is repeated several times sorting, it is impossible to maximized by the functioning efficiency of gravity treatment system, thus this Invention have employed hydrocyclone 1/3 classification underflow and feeds the process of gravity treatment system, coordinates efficient centrifugal reselection simultaneously Equipment, from the point of view of industrial practice effect, has reached the highest efficiency of separation and the response rate, all feeds gravity treatment relative to underflow Process, can significantly save equipment and construction investment, reduces work production and management cost;
2, the present invention uses the centrifugal reselection equipment of high magnification strengthening gravitational field, can realize high concentration ratio and the high efficiency of separation, energy Enough being effectively improved the gold recovery of full factory, increase the economic benefit of enterprise, equipment disposal ability is big simultaneously, and floor space is little, can Reduce workshop capital expenditure cost;
3, the present invention is by reclaiming coarse gold in advance, can reduce and enter the gold mine amount leaching operation, saves the consumption leaching medicament Amount, shortens extraction time, improves the ore treatment ability leaching operation, reduces gold loaded carbon consumption.
Accompanying drawing explanation
Fig. 1 is the FB(flow block) of the embodiment of the present invention.
Detailed description of the invention
Below in conjunction with the accompanying drawings and specific embodiment the present invention is described in further detail.
As it is shown in figure 1, a kind of process reclaiming coarse gold in grinding circuit in advance, this process includes following Step:
Step one, raw ore is put into that to be crushed to granularity in jaw crusher be 0-12mm, namely be crushed to granularity less than 12mm, broken Broken product feeds ball mill by belt conveyor or other load mode and carries out wet milling process, obtains mill discharge, mill Certainly flow to hydrocyclone pump pond obtains slurry to machine discharge;
Step 2, the slurry obtained is delivered to hydrocyclone group by Pulp pump carries out staged care, waterpower in step one The feed pressure of a cluster cyclone is 0.1MPa to 0.18MPa, feed pressure definite in operation need to according to pulp density or other Technological factor is adjusted, and available overflow product and underflow product after hydrocyclone component level, overflow product is particulate portion Point, granularity is that 0-75 μm grade is not less than 85%, and overflow product, after deslagging screen processes, is delivered to concentrate and Cyanide Leaching workshop, Underflow product is coarse component, is emitted into the riffler being located at hydrocyclone group lower end, and riffler includes 1# riffler and 2# Riffler, 1# riffler and 2# riffler are disposed as semi-circular flume structure, 1# riffler and 2# riffler lower end and are respectively provided with Having a desilting pipeline, 1# riffler is connected to ball mill material inlet by a desilting pipeline, and 2# riffler passes through a desilting pipe Road is connected to the vibrosieve material inlet of gravity treatment system, and each hydrocyclone enters one end, ore deposit at it and is provided with valve, passes through water Power cyclone mounting structure configures, and such as water conservancy cyclone installs the difference of quantity, and by Valve controlling hydrocyclone Unlatching quantity, and then regulation and control underflow product enters vibrosieve and the ratio of ball mill, such as, can make the 2/ of underflow product population 3 enter 1# riffler, 1/3 entrance 2# riffler of underflow product population.In 1# riffler and 2# riffler, underflow product enters The ratio of vibrosieve and ball mill can adjust according to the circulating load of grinding system, and Adjustment principle is the thing making entrance gravity treatment system Material ratio is suitable with the new mine-supplying quantity of grinding system, and in the present invention, in 1# and 2# riffler, the allocation proportion of 2:1 is to grind according to routine Ore deposit circulating load 250%-350% is arranged, if circulating load is 200%, then distributes according to the ore pulp of two rifflers of Adjustment principle Ratio need to be adjusted to 1:1.
Underflow product in step 3,2# riffler feeds vibrosieve and carries out sieve classification process, and oversize returns water Power cyclone pump pond, through-screen size is 0-2mm, namely the granularity of undersize is less than 2mm, feeds centrifugal reselection machine and carries out Gravity separation, selects coarse gold, and the mine tailing obtained after gravity separation returns to hydrocyclone pump pond.Centrifugal reselection equipment utilizes 60g high magnification strengthening gravitational field and fluidised Codium fragile (Sur.) Har. dissipate enrichment bed and carry out sorting process, and disposal ability is big, floor space Little, the concentration ratio of Gold Concentrate under Normal Pressure is up to 1000 ~ 3000 times, and the response rate is significantly larger than conventional articulated gravity screening installation.Centrifugal reselection concentrate For high-grade Gold Concentrate under Normal Pressure, mine tailing returns to hydrocyclone pump pond.

Claims (6)

1. the process reclaiming coarse gold in grinding circuit in advance, it is characterised in that: this process includes following Step:
Step one, being 0-12mm by crushing raw ore to granularity, crushed product feeds ball mill and carries out ore grinding process, obtains grinding machine row Material, mill discharge feeds hydrocyclone pump pond and obtains slurry;
Step 2, the slurry obtained is delivered to hydrocyclone group by Pulp pump carries out staged care, waterpower in step one The feed pressure of a cluster cyclone is 0.1MPa to 0.18MPa, obtains overflow product and the end after the classified process of hydrocyclone group Miscarriage product, overflow product, after deslagging screen processes, is delivered to concentrate and Cyanide Leaching workshop, and underflow product is emitted into is located at waterpower The riffler of a cluster cyclone lower end, riffler includes that 1# riffler and 2# riffler, 1# riffler and 2# riffler are disposed as Semi-circular flume structure, 1# riffler is connected to ball mill material inlet by a desilting pipeline, and 2# riffler passes through a desilting pipe Road is connected to the vibrosieve material inlet of gravity treatment system, by the configuration of hydrocyclone mounting structure and Valve controlling hydrocyclone Unlatching quantity, regulation and control underflow product enters vibrosieve and the ratio of ball mill;
Underflow product in step 3,2# riffler feeds vibrosieve and carries out sieve classification process, and oversize returns waterpower rotation Stream device pump pond, through-screen size is 0-2mm, feeds centrifugal reselection machine and carries out gravity separation, selects coarse gold, through gravity separation After the mine tailing that obtains return to hydrocyclone pump pond.
A kind of process reclaiming coarse gold in grinding circuit in advance the most according to claim 1, it is characterised in that: By the configuration of hydrocyclone mounting structure and the unlatching quantity of Valve controlling hydrocyclone, the 2/ of underflow product population can be made 3 enter 1# riffler, 1/3 entrance 2# riffler of underflow product population.
A kind of process reclaiming coarse gold in grinding circuit in advance the most according to claim 1 and 2, its feature exists In: in 1# riffler and 2# riffler, the ratio of underflow product entrance vibrosieve and ball mill can be born according to the circulation of grinding system Lotus adjusts, and Adjustment principle is to make the material ratio mine-supplying quantity new with grinding system of entrance gravity treatment system suitable.
A kind of process reclaiming coarse gold in grinding circuit in advance the most according to claim 1 and 2, its feature exists In: in step 3, centrifugal reselection machine uses 60g gravitational field and fluidised Codium fragile (Sur.) Har. scattered enrichment bed to carry out sorting process.
A kind of process reclaiming coarse gold in grinding circuit in advance the most according to claim 1, it is characterised in that: Crushed product in step one feeds ball mill by belt conveyor and carries out wet milling process.
A kind of process reclaiming coarse gold in grinding circuit in advance the most according to claim 1, it is characterised in that: Mill discharge in step one is from flowing to hydrocyclone pump pond.
CN201610532320.0A 2016-07-08 2016-07-08 A kind of process reclaiming coarse gold in grinding circuit in advance Pending CN106191458A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610532320.0A CN106191458A (en) 2016-07-08 2016-07-08 A kind of process reclaiming coarse gold in grinding circuit in advance

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610532320.0A CN106191458A (en) 2016-07-08 2016-07-08 A kind of process reclaiming coarse gold in grinding circuit in advance

Publications (1)

Publication Number Publication Date
CN106191458A true CN106191458A (en) 2016-12-07

Family

ID=57473627

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610532320.0A Pending CN106191458A (en) 2016-07-08 2016-07-08 A kind of process reclaiming coarse gold in grinding circuit in advance

Country Status (1)

Country Link
CN (1) CN106191458A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108187878A (en) * 2017-12-29 2018-06-22 潘自维 A kind of one and half closed circuit grinding grading techniques
CN109731668A (en) * 2019-02-15 2019-05-10 赤峰柴胡栏子黄金矿业有限公司 The method of tailings total cyanogen concentration is reduced in a kind of gold mine ore dressing process

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104152711A (en) * 2014-08-06 2014-11-19 哈巴河金坝矿业有限公司 Method and device for performing all-mud cyaniding recycling on gold ores
CN104174482A (en) * 2014-09-03 2014-12-03 鞍钢集团矿业公司 Mineral processing technology for low grade hematite ore
CN104307626A (en) * 2014-10-13 2015-01-28 中国瑞林工程技术有限公司 Dressing technology for recycling ultra-low-level gold ore
CN104492615A (en) * 2014-10-31 2015-04-08 四川安宁铁钛股份有限公司 Grinding classification method
CN105536981A (en) * 2015-12-14 2016-05-04 灵宝金源晨光有色矿冶有限公司 Process for recovering gold, silver and sulfur from castaway slag

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104152711A (en) * 2014-08-06 2014-11-19 哈巴河金坝矿业有限公司 Method and device for performing all-mud cyaniding recycling on gold ores
CN104174482A (en) * 2014-09-03 2014-12-03 鞍钢集团矿业公司 Mineral processing technology for low grade hematite ore
CN104307626A (en) * 2014-10-13 2015-01-28 中国瑞林工程技术有限公司 Dressing technology for recycling ultra-low-level gold ore
CN104492615A (en) * 2014-10-31 2015-04-08 四川安宁铁钛股份有限公司 Grinding classification method
CN105536981A (en) * 2015-12-14 2016-05-04 灵宝金源晨光有色矿冶有限公司 Process for recovering gold, silver and sulfur from castaway slag

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
《贵金属生产技术实用手册》编委会: "《贵金属生产技术实用手册》", 31 January 2011 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108187878A (en) * 2017-12-29 2018-06-22 潘自维 A kind of one and half closed circuit grinding grading techniques
CN108187878B (en) * 2017-12-29 2021-02-02 中业纳米科技(烟台)有限公司 One-section semi-closed-circuit ore grinding and grading process
CN109731668A (en) * 2019-02-15 2019-05-10 赤峰柴胡栏子黄金矿业有限公司 The method of tailings total cyanogen concentration is reduced in a kind of gold mine ore dressing process

Similar Documents

Publication Publication Date Title
CN101219413B (en) Technique for manufacturing hyperpure iron extract
CN109331989B (en) Dry dewatering and deashing process for coal full-size fraction
CN104470646B (en) The method and apparatus of separating granular
CN203791036U (en) Coarse slime dense medium separation system
CN201676741U (en) Desliming type liquid-solid fluidized bed coarse slime sorting and grading device
CN105251572A (en) Novel ore grinding classification system and process
CN101869877A (en) Coal gangue sorting process
CN102319619A (en) Graded washing process for raw coal
CN106391298A (en) Closed circuit ore grinding classification method
CN106216082A (en) Low-grade Anshan type iron mine composite ore ore-dressing technique
CN101850293A (en) Coarse coal slime sorting and grading plant for desliming type liquid-solid fluid bed
CN103691538B (en) A kind of grinding classification system of Ore
CN104492615A (en) Grinding classification method
CN107661814B (en) Screening-magnetic separation-ore grinding-magnetic separation flow equipment arrangement system
CN110385197B (en) Gravity separation system and process for barite fluorite associated ore
CN102228866B (en) Compound classification method and equipment for ground ore product
CN106191458A (en) A kind of process reclaiming coarse gold in grinding circuit in advance
CN101274298A (en) Anshan style lean hematite swirler-lattice type ball mill primary closed-circuit grinding grading technique
CN100563838C (en) Mine tailing reclaims sulphur iron separation ore-sorting system and method
CN203874891U (en) Backwater feed device with fractional concentration function
CN103752428A (en) Beneficiation method of vanadium titano-magnetite
CN106391292A (en) Liquid-solid fluidized bed sorting machine and material sorting method employing same
CN105170283A (en) Ore grinding grading system and method capable of controlling derichment of iron minerals
CN104958949A (en) Multi-distribution system of tailings dry discharge belt filtering machine
CN104785359B (en) A kind of mobile ore dressing plant

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20161207