CN103433123A - Process for ore pulp desliming and ore slurry dehydration - Google Patents

Process for ore pulp desliming and ore slurry dehydration Download PDF

Info

Publication number
CN103433123A
CN103433123A CN2013104190640A CN201310419064A CN103433123A CN 103433123 A CN103433123 A CN 103433123A CN 2013104190640 A CN2013104190640 A CN 2013104190640A CN 201310419064 A CN201310419064 A CN 201310419064A CN 103433123 A CN103433123 A CN 103433123A
Authority
CN
China
Prior art keywords
ore
desliming
ore pulp
slurry
sludge
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
CN2013104190640A
Other languages
Chinese (zh)
Inventor
胡晓军
张玉胜
沈宾
于栋
梁勇
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.)
JIANGSU MYANDE FOOD MACHINERY Co Ltd
Original Assignee
JIANGSU MYANDE FOOD MACHINERY 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 JIANGSU MYANDE FOOD MACHINERY Co Ltd filed Critical JIANGSU MYANDE FOOD MACHINERY Co Ltd
Priority to CN2013104190640A priority Critical patent/CN103433123A/en
Publication of CN103433123A publication Critical patent/CN103433123A/en
Pending legal-status Critical Current

Links

Images

Landscapes

  • Paper (AREA)

Abstract

The invention provides a process for ore pulp desliming and ore slurry dehydration, which relates to a mineral processing process. The process comprises the steps of: a, removing large dreg of ore pulp raw materials by using a dreg separation sieve; b, removing impurities of the ore pulp raw materials without the large dreg by adopting a sorting filter and enabling the ore pulp raw materials to enter a sorting machine to be subjected to desliming and selection to obtain deslimed ore pulp and ore slurry; c, enabling the deslimed ore pulp to enter a floating selection procedure; after removing the impurities of the ore slurry with a dehydrating filter, enabling the ore slurry to enter a dehydrating machine to be concentrated and dehydrated so as to obtain concentrated ore slurry and reusable process pure water. The process is simple and reliable; the concentration and the grade of the ore slurry are improved and the desliming is complete; rapid concentration and dehydration of the ore slurry are realized; the process has important effects in the aspects of improving the stability of selection work and the grade and the recovery rate of ore concentrates, reducing the use amounts of a floating selection medicament and pure water and the like.

Description

The technique of a kind of ore pulp desliming and sludge dehydration
Technical field
The present invention relates to a kind of ore-dressing technique, be specially the technique of a kind of ore pulp desliming and sludge dehydration.
Background technology
Sludge in the ore dressing term refers generally to the grade material of granularity<10um, according to current ore-dressing technique level, in selected material<the 10um grade is difficult to effective recovery, and assorting room disturbed, affect concentrate taste and the rate of recovery, increase reagent consumption.Therefore, the high material for clay content, should need to remove in advance sludge wherein according to technique, main desliming bucket or two kinds of equipment of water conservancy cyclone of adopting carry out desliming at present, but its desliming efficiency is lower, selected material clay content is higher, purpose mineral loss late is bigger than normal, is unfavorable for the raising of technique of preparing economic indicator.At present desliming process commonly used is to adopt water conservancy cyclone to carry out a desliming, in its sand setting (or underflow)<the 10um grain size content is generally 20 ~ 30%, in overflow>the 10um grain size content is generally more than 30%.The classification matter efficiency of a desliming process of hydrocyclone is 50% left and right only,>10um grade loss late 20% left and right, and the desliming effect of desliming bucket is poorer.
Summary of the invention
The objective of the invention is to solve that current desliming process is complicated, the poor problem of effect, a kind of efficient desliming, dewatering process are provided, can will be selected in the material clay content and purpose mineral loss late reduces greatly.
The technical scheme that realizes above-mentioned purpose is: the technique of a kind of ore pulp desliming and sludge dehydration is characterized in that: comprise the following steps: a, by raw material of ore by remove large slag every ballast screen; B, except the raw material of ore after large slag enters separator after the impurity elimination of sorting filter, carry out desliming and selected, obtain desliming ore pulp and sludge slurry; C, desliming ore pulp enter flotation process, and the sludge slurry enters dewaterer and concentrates and dewater after the dehydrator filter impurities removal, obtain thickened slurry slurry and recycling technique water purification.
Above-mentioned separator is the disc type separator, and above-mentioned dewaterer is disk type dehydrator.
This simple and reliable process, improved pulp density and grade, and desliming is thorough, and realized the concentrated and dehydration fast of sludge slurry; For the aspects such as stability, concentrate grade and the rate of recovery, reduction floating agent and water purification consumption that improve sorting operation, play an important role.
The accompanying drawing explanation
Fig. 1 is process chart of the present invention.
The specific embodiment
Illustrate implementation step of the present invention below in conjunction with accompanying drawing 1:
A, by raw material of ore by every ballast screen 1, removing large slag, send into ore pulp tank 2 except after large slag;
B, by ore pulp feed pump 3 by 4 impurity eliminations of the raw material of ore in ore pulp tank 2 input sorting filter;
C, the input of the raw material of ore after 4 impurity eliminations of sorting filter separator 5 carry out desliming and selected, obtain desliming ore pulp and sludge slurry, and the desliming ore pulp enters flotation process, and the sludge slurry is sent into ore deposit slurry tank 6;
Sludge slurry in d, ore deposit slurry tank 6 is starched feed pump 7 input dehydrator filter 8 impurities removals by sludge, and the sludge slurry enters dewaterer 9 and concentrates and dewater after dehydrator filter 8 impurities removals, obtains thickened slurry slurry and recycling technique water purification.
Above-mentioned separator 5 is the disc type separator, and above-mentioned dewaterer 9 is disk type dehydrator; Disc type separator and disk type dehydrator are disk centrifugal separator of the prior art, at this, are not repeating.

Claims (3)

1. the technique of an ore pulp desliming and sludge dehydration is characterized in that: comprise the following steps: a, by raw material of ore by remove large slag every ballast screen; B, except the raw material of ore after large slag enters separator after the impurity elimination of sorting filter, carry out desliming and selected, obtain desliming ore pulp and sludge slurry; C, desliming ore pulp enter flotation process, the sludge slurry enters dewaterer and concentrates and dewater after the dehydrator filter impurities removal, obtain thickened slurry slurry and recycling technique water purification.
2. the technique that a kind of ore pulp desliming according to claim 1 and sludge dewater, it is characterized in that: described separator is the disc type separator.
3. the technique that a kind of ore pulp desliming according to claim 1 and sludge dewater, it is characterized in that: described dewaterer is disk type dehydrator.
CN2013104190640A 2013-09-16 2013-09-16 Process for ore pulp desliming and ore slurry dehydration Pending CN103433123A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2013104190640A CN103433123A (en) 2013-09-16 2013-09-16 Process for ore pulp desliming and ore slurry dehydration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2013104190640A CN103433123A (en) 2013-09-16 2013-09-16 Process for ore pulp desliming and ore slurry dehydration

Publications (1)

Publication Number Publication Date
CN103433123A true CN103433123A (en) 2013-12-11

Family

ID=49686892

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2013104190640A Pending CN103433123A (en) 2013-09-16 2013-09-16 Process for ore pulp desliming and ore slurry dehydration

Country Status (1)

Country Link
CN (1) CN103433123A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104083939A (en) * 2014-07-10 2014-10-08 云南大红山管道有限公司 Iron ore concentrate pulp dehydration system
CN105214380A (en) * 2015-11-02 2016-01-06 迈安德集团有限公司 A kind of microfine pulp thickening system and slurry concentrating technique
CN105214854A (en) * 2015-11-02 2016-01-06 迈安德集团有限公司 A kind of micro-size fraction dry-discharge system for tailings and tailing dry-type emission technology
CN105214833A (en) * 2015-11-02 2016-01-06 迈安德集团有限公司 A kind of cyclone overflow pulp hierarchy system and ore pulp grading technology
CN105233973A (en) * 2015-11-02 2016-01-13 迈安德集团有限公司 Graded desliming system and process for mica
CN105233971A (en) * 2015-11-02 2016-01-13 迈安德集团有限公司 Baffle-plate overflowing ore pulp grading system and ore pulp grading process
CN105344465A (en) * 2015-11-02 2016-02-24 迈安德集团有限公司 Ore pulp de-sliming system and ore pulp de-sliming technology
CN105642432A (en) * 2016-03-09 2016-06-08 旌德县圣裕莹石加工有限公司 Unit used for machining fluorite mineral aggregate and application thereof
CN106311455A (en) * 2016-08-25 2017-01-11 湖南顺源陶瓷材料有限公司 Desliming process for nonmetal mineral separation
CN113908972A (en) * 2020-07-10 2022-01-11 中蓝连海设计研究院有限公司 Method for recovering fine slime ore in phosphorite slime

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62225591A (en) * 1986-03-27 1987-10-03 Sumitomo Heavy Ind Ltd Production of deashed and fine powdered coal slurry in high concentration
CN102489385A (en) * 2011-12-12 2012-06-13 云南三明鑫疆矿业有限公司 Combined technology of phosphorite scrubbing and direct floatation and reverse floatation
CN202725309U (en) * 2012-09-01 2013-02-13 山东科技大学 Coarse slime separation system
CN202752094U (en) * 2012-08-22 2013-02-27 山西晋城无烟煤矿业集团有限责任公司 Pulverized coal slime dehydration system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62225591A (en) * 1986-03-27 1987-10-03 Sumitomo Heavy Ind Ltd Production of deashed and fine powdered coal slurry in high concentration
CN102489385A (en) * 2011-12-12 2012-06-13 云南三明鑫疆矿业有限公司 Combined technology of phosphorite scrubbing and direct floatation and reverse floatation
CN202752094U (en) * 2012-08-22 2013-02-27 山西晋城无烟煤矿业集团有限责任公司 Pulverized coal slime dehydration system
CN202725309U (en) * 2012-09-01 2013-02-13 山东科技大学 Coarse slime separation system

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
周忠琴等: "炼焦煤选煤厂的煤泥水深度澄清", 《洁净煤技术》 *
符福存: "对选煤厂设计的几点看法", 《煤炭加工与综合利用》 *

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104083939A (en) * 2014-07-10 2014-10-08 云南大红山管道有限公司 Iron ore concentrate pulp dehydration system
CN105214380A (en) * 2015-11-02 2016-01-06 迈安德集团有限公司 A kind of microfine pulp thickening system and slurry concentrating technique
CN105214854A (en) * 2015-11-02 2016-01-06 迈安德集团有限公司 A kind of micro-size fraction dry-discharge system for tailings and tailing dry-type emission technology
CN105214833A (en) * 2015-11-02 2016-01-06 迈安德集团有限公司 A kind of cyclone overflow pulp hierarchy system and ore pulp grading technology
CN105233973A (en) * 2015-11-02 2016-01-13 迈安德集团有限公司 Graded desliming system and process for mica
CN105233971A (en) * 2015-11-02 2016-01-13 迈安德集团有限公司 Baffle-plate overflowing ore pulp grading system and ore pulp grading process
CN105344465A (en) * 2015-11-02 2016-02-24 迈安德集团有限公司 Ore pulp de-sliming system and ore pulp de-sliming technology
CN105214854B (en) * 2015-11-02 2017-08-08 迈安德集团有限公司 A kind of micro-size fraction dry-discharge system for tailings and tailing dry-type emission technology
CN105214833B (en) * 2015-11-02 2017-08-08 迈安德集团有限公司 A kind of cyclone overflow pulp hierarchy system and ore pulp grading technology
CN105642432A (en) * 2016-03-09 2016-06-08 旌德县圣裕莹石加工有限公司 Unit used for machining fluorite mineral aggregate and application thereof
CN106311455A (en) * 2016-08-25 2017-01-11 湖南顺源陶瓷材料有限公司 Desliming process for nonmetal mineral separation
CN113908972A (en) * 2020-07-10 2022-01-11 中蓝连海设计研究院有限公司 Method for recovering fine slime ore in phosphorite slime

Similar Documents

Publication Publication Date Title
CN103433123A (en) Process for ore pulp desliming and ore slurry dehydration
CN103464272B (en) A kind of coarse slime two sections of water Jie method for separating
CN110201791B (en) Comprehensive utilization method of sandy kaolin tailings containing tourmaline, muscovite and quartz sand
CN111659527B (en) Gasification slag water medium cyclone gravity carbon ash separation device and method
CN102284354B (en) Coarse slime separating process
CN102728455B (en) Combined separation process for gravity concentration and flotation of difficult separation coal slime with high intermediate density material content
CN102319614A (en) Benefication method for recovering ilmenite from iron tailings in Shandong area
CN103301679A (en) Tailing dewatering method
CN102069033A (en) Method for separating and extracting feldspar ore with complex impurity components
CN104941780A (en) Mineral processing technology capable of effectively separating tantalum, tin and lepidomelane
CN102228762A (en) Dehydration method and device of tailings
CN104475238B (en) A kind of enrichment method of appositional pattern navajoite
CN104437828A (en) Efficient desulfuration and deashing dense medium separation technology for fine coal
CN103212478A (en) Floating magnetic combined ore dressing process for recovering mica from iron ore mill tailings
CN100444964C (en) Benefication of magnetite-haematite acid mixed mine
CN109847923B (en) Recovery process of extremely-poor weathered primary ilmenite
CN101254375A (en) Dewatering process screening fine ore of alumyte
CN110404665A (en) A kind of processing method of ultra-fine coal slurry dehydration
CN202881039U (en) Integrated treatment system for coal deep-well mine water treatment
CN213161291U (en) Equipment for sorting bauxite ore
CN112138856B (en) All-magnetic separation process for gangue-combined media in easily-argillized power coal
CN113546750A (en) Two-stage wet mica removing process for machine-made sand
CN203540734U (en) Recovery device of refractory coal slime with high ash content
CN103214112A (en) Treatment method of limestone tailings water
CN202143801U (en) Tailing dehydrating device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20131211