CN105858628B - A kind of method for improving mid low grade phosphate rock extraction yield - Google Patents

A kind of method for improving mid low grade phosphate rock extraction yield Download PDF

Info

Publication number
CN105858628B
CN105858628B CN201610400415.7A CN201610400415A CN105858628B CN 105858628 B CN105858628 B CN 105858628B CN 201610400415 A CN201610400415 A CN 201610400415A CN 105858628 B CN105858628 B CN 105858628B
Authority
CN
China
Prior art keywords
low grade
phosphate rock
grade phosphate
mid low
dispersant
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
CN201610400415.7A
Other languages
Chinese (zh)
Other versions
CN105858628A (en
Inventor
王福忠
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.)
Yunnan Tianning Mining Co ltd
Original Assignee
Fujian Province Druze Oil 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 Fujian Province Druze Oil Co Ltd filed Critical Fujian Province Druze Oil Co Ltd
Priority to CN201610400415.7A priority Critical patent/CN105858628B/en
Publication of CN105858628A publication Critical patent/CN105858628A/en
Application granted granted Critical
Publication of CN105858628B publication Critical patent/CN105858628B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/01Treating phosphate ores or other raw phosphate materials to obtain phosphorus or phosphorus compounds
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B25/00Phosphorus; Compounds thereof
    • C01B25/16Oxyacids of phosphorus; Salts thereof
    • C01B25/18Phosphoric acid
    • C01B25/22Preparation by reacting phosphate-containing material with an acid, e.g. wet process
    • C01B25/222Preparation by reacting phosphate-containing material with an acid, e.g. wet process with sulfuric acid, a mixture of acids mainly consisting of sulfuric acid or a mixture of compounds forming it in situ, e.g. a mixture of sulfur dioxide, water and oxygen

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • Compounds Of Alkaline-Earth Elements, Aluminum Or Rare-Earth Metals (AREA)

Abstract

The present invention relates to a kind of method for improving mid low grade phosphate rock extraction yield, mid low grade phosphate rock stone is added in disintegrating machine and first slightly broken, mid low grade phosphate rock stone after slightly breaking enters ball mill, water and dispersant are added in ball mill simultaneously, by mid low grade phosphate rock stone ball milling into ore pulp, ore pulp is squeezed into extraction tank and extracted, and phosphoric acid is made, and detects the extraction yield of phosphorus ore.The addition that this method passes through dispersant, the flocculation between ore pulp and ore pulp after ball milling and between ore pulp and extraction accessory substance ardealite in extraction process can be prevented, the specific surface area that ore contacts with dilute sulfuric acid is improved, so as to effectively improve the extraction yield of phosphorus ore, and saves extraction time.

Description

A kind of method for improving mid low grade phosphate rock extraction yield
Technical field
The present invention relates to a kind of method for improving mid low grade phosphate rock extraction yield.
Background technology
China's phosphorus ore reserves are big, occupy the second in the world, and its feature is that rich ore is few, and middle and low grade bauxite is more.But in recent years, due to The increase of high-concentration compound fertilizer yield, phosphorus ore day of the content more than 30% are becoming tight.And the two water laws production phosphorus that China is traditional Acid is, it is necessary to using P2O5>=30% high-grade ore, extraction yield can reach more than 99%, P2O5≤ 30% mid low grade phosphate rock, Due to more containing impurity, if directly extracting, extraction yield is generally below 96%, causes the wasting of resources, and mid low grade phosphate rock needs Purification by floatation rear can be used.At present there has been no can be by directly extracting mid low grade phosphate rock, the method for improving extraction yield.
The content of the invention
The technical problem to be solved by the invention is to provide a kind of method for improving mid low grade phosphate rock extraction yield.The party Method can significantly improve the extraction yield of low-grade phosphate ore, reduce enterprise's production cost, economize on resources.
In order to solve the above-mentioned technical problem, the present invention uses following technical scheme:
A kind of method for improving mid low grade phosphate rock extraction yield, it is characterised in that follow the steps below:
1), mid low grade phosphate rock stone is put into disintegrating machine and slightly broken, obtain product A;
2), water, dispersant and product A be added separately in ball mill according to certain mass ratio, carry out ball milling in the lump and beat Slurry;
3), by step 2)The slurry of preparation is squeezed into extraction tank, is extracted with sulfuric acid, and phosphoric acid is made;
Wherein product A, water, dispersant, the mass ratio of sulfuric acid are 35~50:10~30:0.2~2:25~50;
Described mid low grade phosphate rock stone refers to less than 24%~30%;
The dispersant is HPMA, Sodium Polyacrylate and one kind or arbitrary proportion in 5040 dispersants It is two or more;The sulfuric acid concentration is 65%.
The dispersant is that HPMA and Sodium Polyacrylate compounding form, HPMA and polypropylene Sour sodium mass ratio is 3:2.
Wherein the mass ratio of product A, water, dispersant and sulfuric acid is 40:17:1:42.
The present invention has following advantageous effects:
1st, this method can prevent between ore pulp and ore pulp after ball milling by the addition of dispersant and ore pulp is secondary with extracting Flocculation between product ardealite in extraction process, the specific surface area that ore contacts with dilute sulfuric acid is improved, so as to effectively improve The extraction yield of phosphorus ore, and save extraction time, extraction yield is up to more than 97.5%.
2nd, present invention process is simple, only carries out simply transforming on existing equipment, will not cause to bear to enterprise.
3rd, the present invention can significantly improve low-grade phosphate ore extraction yield, can solve the problems, such as low-grade phosphate ore using difficult, drop Low entreprise cost, economizes on resources.
Embodiment
The present invention is further illustrated with reference to instantiation.
Embodiment 1
The low-grade phosphate ore stone of content 25.4% is added in disintegrating machine and first slightly broken, the rock phosphate in powder after slightly breaking is direct Into ball mill, while water and dispersant are added in ball mill, by rock phosphate in powder ball milling into ore pulp, ore pulp is squeezed into sharp in extraction tank Extracted with sulfuric acid, phosphoric acid is made.
Rock phosphate in powder, water, HPMA, Sodium Polyacrylate, the mass ratio of 5040 dispersants and sulfuric acid are:40:17: 0.6:0.4:0.3:41.7。
The extraction yield for detecting phosphorus ore is 98.2%.
Embodiment 2
The low-grade phosphate ore stone of content 25.4% is added in disintegrating machine and first slightly broken, the rock phosphate in powder after slightly breaking is direct Into ball mill, while water and dispersant are added in ball mill, by rock phosphate in powder ball milling into ore pulp, ore pulp is squeezed into sharp in extraction tank Extracted with sulfuric acid, phosphoric acid is made.
Rock phosphate in powder, water, HPMA, Sodium Polyacrylate, the mass ratio of 5040 dispersants and sulfuric acid are:40:17: 0.6:0.4:42。
The extraction yield for detecting phosphorus ore is 98.6%.
Embodiment 3
The low-grade phosphate ore stone of content 25.4% is added in disintegrating machine and first slightly broken, the rock phosphate in powder after slightly breaking is direct Into ball mill, while water and dispersant are added in ball mill, by rock phosphate in powder ball milling into ore pulp, ore pulp is squeezed into sharp in extraction tank Extracted with sulfuric acid, phosphoric acid is made.
Rock phosphate in powder, water, HPMA, the mass ratio of Sodium Polyacrylate and sulfuric acid are:40:17:0.4:0.6:42.
The extraction yield for detecting phosphorus ore is 97.8%.
Embodiment 4
The low-grade phosphate ore stone of content 25.4% is added in disintegrating machine and first slightly broken, the rock phosphate in powder after slightly breaking is direct Into ball mill, while water and dispersant are added in ball mill, by rock phosphate in powder ball milling into ore pulp, ore pulp is squeezed into sharp in extraction tank Extracted with sulfuric acid, phosphoric acid is made.
Rock phosphate in powder, water, the mass ratio of 5040 dispersants and sulfuric acid are:40:17:1:42.
The extraction yield for detecting phosphorus ore is 98.2%.
Beneficial effect of the present invention is further illustrated with reference to experimental data:
By taking embodiment 2 as an example, conventional extraction (removing non-bonus point powder, other working conditions are consistent with embodiment 2) and implementation Example 2 equally detects the results contrast of three order of classes or grades at school of each production, testing result such as table 1
Table 1
Day shift The middle class in a kindergarten Night shift
Conventional extraction extraction yield (%) 95.7 95.1 95.2
The extraction yield of embodiment 2 (%) 98.7 98.4 98.7
Extraction yield of the extraction yield of embodiment 2 apparently higher than conventional extraction as can be seen from Table 1.This method through continuous production not It was found that there are other problems, it has been applied at present.
Discuss:Find the filtering of the ardealite of by-product of the present invention significantly better than the work for being not added with dispersant through continuous production Skill, there may be some characteristics of surfactant with dispersant, contribute to the growth of ardealite crystal, forming thick rod crystalline substance has Close, currently among research.

Claims (3)

  1. A kind of 1. method for improving mid low grade phosphate rock extraction yield, it is characterised in that follow the steps below:
    1), mid low grade phosphate rock stone is put into disintegrating machine and slightly broken, obtain product A;
    2), water, dispersant and product A be added separately in ball mill according to certain mass ratio, carry out ball milling mashing in the lump;
    3), by step 2)The slurry of preparation is squeezed into extraction tank, is extracted with sulfuric acid, and phosphoric acid is made;
    Wherein product A, water, dispersant, the mass ratio of sulfuric acid are 35~50:10~30:0.2~2:25~50;
    Described mid low grade phosphate rock stone refers to less than 24%~30%;
    The dispersant is HPMA, Sodium Polyacrylate and one kind in 5040 dispersants or two kinds of arbitrary proportion More than;The sulfuric acid concentration is 65%.
  2. 2. the method according to claim 1 for improving mid low grade phosphate rock extraction yield, it is characterised in that:The dispersant is HPMA and Sodium Polyacrylate compounding form, and HPMA and Sodium Polyacrylate mass ratio are 3:2.
  3. 3. the method according to claim 1 for improving mid low grade phosphate rock extraction yield, it is characterised in that:Wherein product A, The mass ratio of water, dispersant and sulfuric acid is 40:17:1:42.
CN201610400415.7A 2016-06-08 2016-06-08 A kind of method for improving mid low grade phosphate rock extraction yield Expired - Fee Related CN105858628B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610400415.7A CN105858628B (en) 2016-06-08 2016-06-08 A kind of method for improving mid low grade phosphate rock extraction yield

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610400415.7A CN105858628B (en) 2016-06-08 2016-06-08 A kind of method for improving mid low grade phosphate rock extraction yield

Publications (2)

Publication Number Publication Date
CN105858628A CN105858628A (en) 2016-08-17
CN105858628B true CN105858628B (en) 2018-02-09

Family

ID=56676121

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610400415.7A Expired - Fee Related CN105858628B (en) 2016-06-08 2016-06-08 A kind of method for improving mid low grade phosphate rock extraction yield

Country Status (1)

Country Link
CN (1) CN105858628B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107983539A (en) * 2017-12-06 2018-05-04 中南大学 Application of the hydrolysis of polymaleic anhydride in Scheelite Flotation

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1699148A (en) * 2004-05-21 2005-11-23 李兴才 Process for producing industrial phosphoric acid using phosphorus ore as raw material
CN102643629A (en) * 2012-04-06 2012-08-22 湖北富邦科技股份有限公司 Grinding aid for phosphate rock

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1699148A (en) * 2004-05-21 2005-11-23 李兴才 Process for producing industrial phosphoric acid using phosphorus ore as raw material
CN102643629A (en) * 2012-04-06 2012-08-22 湖北富邦科技股份有限公司 Grinding aid for phosphate rock

Also Published As

Publication number Publication date
CN105858628A (en) 2016-08-17

Similar Documents

Publication Publication Date Title
CN103706485B (en) A kind of beneficiation method of high carbon acid calcium type fluorite ore
CN103464288A (en) Method for removing silicon from phosphogypsum in obverse floatation way under acidic condition
CN102716806B (en) Method for simultaneously removing magnesium oxide, ferric oxide and aluminum oxide sesquioxide in middle-grade and low-grade phosphate ores by adopting double-reverse flotation process
US20180043373A1 (en) Collector for beneficiating carbonaceous phosphate ores
CN105600763B (en) A kind of method that fluoride salt method of purification produces industrial monoammonium phosphate
CN106744753B (en) A kind of method of phosphorus ore stagewise de-magging
CN105689150A (en) Lead-zinc oxide ore flotation inhibitor and application thereof
CN109261366A (en) A kind of combination medicament and its application method removing calcite in advance for high calcium fluorite reverse flotation
CN109772590B (en) Collecting agent for flotation decalcification of magnesite and application thereof
CN104229764A (en) Method for continuously producing water-soluble monoammonium phosphate by using wet-process phosphoric acid
CN103691567A (en) Flotation separation method of fluorite and dolomite in acidic conditions
CN104801427A (en) Direct and reverse flotation technique for high-magnesium low-grade phosphorus ore coarse grains
CN104174504A (en) Direct-flotation branching floatation method of low-and-medium-grade mixed type refractory collophane
CN101565188B (en) Technique for preparing borax from brine
CN105858628B (en) A kind of method for improving mid low grade phosphate rock extraction yield
CN112221718B (en) Collecting agent applied to normal-temperature alkali-free flotation of collophanite and preparation method thereof
CN103030124B (en) Method for preparing food-grade phosphoric acid from medium/low-grade phosphorite
CN102674405A (en) Method for preparing potassium sulfate by using picromerite
CN104261371B (en) A kind of method by high impurity phosphorus ore production diammonium phosphate
CN111036415A (en) Application of inhibitor HEDP in magnesite direct flotation decalcification
CN102030321B (en) Method for producing fertilizer with high feedstuff-fertilizer ratio by utilizing low-grade phosphate ores
CN102659454A (en) Method for preparing diammonium phosphate and slow release fertilizer by using high-impurity phosphorite
CN106045705A (en) Method for producing spray organic and inorganic composite fertilizer from middle-and-low-grade phosphate ore
CN111036413B (en) Application of inhibitor AA/AMPS in positive flotation and magnesium removal of phosphate ore
CN103011671A (en) Method for separating concrete water reducing agent of crystalline silicon cutting liquid mortar

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
CB03 Change of inventor or designer information
CB03 Change of inventor or designer information

Inventor after: Wang Fuzhong

Inventor before: Ji Xinqiang

TA01 Transfer of patent application right

Effective date of registration: 20171225

Address after: 362000 Lingshan Industrial Zone, Tu Town, Quanzhou County, Fujian, Huian

Applicant after: FUJIAN DELUSHI LUBRICATING OIL Co.,Ltd.

Address before: No. 71, Xicheng village, Yantai, Zhaoyuan City, Zhaoyuan, Shandong

Applicant before: Ji Xinqiang

TA01 Transfer of patent application right
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20191210

Address after: No.322, building 4, Zone 8, hengtaiyun shopping mall, Nanxiang, Yongqiao District, Suzhou City, Anhui Province

Patentee after: Suzhou Ziyuan Science and Technology Consulting Co.,Ltd.

Address before: 362000 Lingshan Industrial Zone, Tu Town, Quanzhou County, Fujian, Huian

Patentee before: FUJIAN DELUSHI LUBRICATING OIL Co.,Ltd.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20200226

Address after: 650300 xiayuanliang village, County Street office, Anning City, Kunming City, Yunnan Province

Patentee after: Yunnan Tianning Mining Co.,Ltd.

Address before: No.322, building 4, Zone 8, hengtaiyun shopping mall, Nanxiang, Yongqiao District, Suzhou City, Anhui Province

Patentee before: Suzhou Ziyuan Science and Technology Consulting Co.,Ltd.

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

Granted publication date: 20180209

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