SU698654A1 - Method of concentrating caolines and clays - Google Patents
Method of concentrating caolines and claysInfo
- Publication number
- SU698654A1 SU698654A1 SU772559229A SU2559229A SU698654A1 SU 698654 A1 SU698654 A1 SU 698654A1 SU 772559229 A SU772559229 A SU 772559229A SU 2559229 A SU2559229 A SU 2559229A SU 698654 A1 SU698654 A1 SU 698654A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- sodium
- concentrate
- ammonium salts
- humic acids
- kaolin
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 12
- 235000012211 aluminium silicate Nutrition 0.000 claims description 7
- 239000005995 Aluminium silicate Substances 0.000 claims description 5
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 5
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 5
- 235000019353 potassium silicate Nutrition 0.000 claims description 5
- 239000011734 sodium Substances 0.000 claims description 5
- 229910052708 sodium Inorganic materials 0.000 claims description 5
- 239000012736 aqueous medium Substances 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 239000000725 suspension Substances 0.000 claims description 4
- 239000004927 clay Substances 0.000 claims description 3
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 2
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 230000018044 dehydration Effects 0.000 claims description 2
- 238000006297 dehydration reaction Methods 0.000 claims description 2
- 239000002245 particle Substances 0.000 claims description 2
- 229910052710 silicon Inorganic materials 0.000 claims description 2
- 239000010703 silicon Substances 0.000 claims description 2
- 150000003863 ammonium salts Chemical class 0.000 claims 4
- 239000012141 concentrate Substances 0.000 claims 4
- 239000004021 humic acid Substances 0.000 claims 4
- 229910000323 aluminium silicate Inorganic materials 0.000 claims 2
- 239000007884 disintegrant Substances 0.000 claims 2
- 238000000605 extraction Methods 0.000 claims 2
- 239000007787 solid Substances 0.000 claims 2
- 239000003153 chemical reaction reagent Substances 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 230000003247 decreasing effect Effects 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000004519 manufacturing process Methods 0.000 claims 1
- 239000000463 material Substances 0.000 claims 1
- 238000001935 peptisation Methods 0.000 claims 1
- 238000011084 recovery Methods 0.000 claims 1
- 238000001694 spray drying Methods 0.000 claims 1
- 239000002699 waste material Substances 0.000 claims 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 235000010755 mineral Nutrition 0.000 description 2
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- -1 crushing Chemical compound 0.000 description 1
- 230000008021 deposition Effects 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 159000000001 potassium salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
Description
II
Изобретение касаетс обогащени минерального сырь и относитс к технологии получени гомогенизированных обогащенных каолинов и глчн в гранулированном виде,, которые могут использоватьс на каолино- и глинообогатительных фабриках, в керамической, бумажной , химической и других отрасл х промыщленности.The invention relates to the enrichment of mineral raw materials and relates to the technology of producing homogenized enriched kaolins and glossy in granular form, which can be used in kaolite and ore processing plants, in the ceramic, paper, chemical and other industries.
Известен способ обогащени каолинов и глин в присутствии реагентов ионизителей в зкости, создающих услови дл быстрого роспуска сырь в водной среде и последующего разделени суспензий по крупности l. .A known method of enriching kaolin and clay in the presence of viscosity ionizing agents, which create conditions for the rapid dissolution of raw materials in an aqueous medium and the subsequent separation of suspensions according to particle size l. .
В качестве пептизаторов обычно примен ют натриевые или калиевые соли неорганических кислот, например, жидкое стекло, фосфаты, едкий натр.Sodium or potassium salts of inorganic acids, for example, liquid glass, phosphates, caustic soda, are commonly used as peptizers.
Недостаток такого способа обогащени заключаетс в сложности процесса обогащени и высоких дополнительных затратах в переделе обогащениThe disadvantage of this method of enrichment lies in the complexity of the enrichment process and the high additional costs in redistributing the enrichment process.
Наиболее близким по технической сущности к изобретению вл етс способ обогащени каолинов и глин, включающий дробление, дезинтеграцию в водной среде в присутствии пептизатора жидкого стекла с кремниевым модулем 2-3,5, классификацию пульпы по крупности н обезвоживание 2.The closest to the technical essence of the invention is a method of enrichment of kaolin and clay, including crushing, disintegration in an aqueous medium in the presence of a peptizer of liquid glass with a silicon module of 2-3.5, the classification of pulp by size n dehydration 2.
Недостатки этого способа обогащени заключаютс в сложности процесса обогащени , обусловленной необходимостью подогрева пульпы в операции дезинтеграции острым паром до 4О6О С, вызывающей дополнительные затраты в переделе обог .щени , высокий расход жидкого стекла, обусловленный необходимостью создани рН среды до 9,5-10 и выше, который приводит к осаждению его на внутренних стенках трубопроводов, насосов и обогатительного оборудовани .The disadvantages of this enrichment process are the complexity of the enrichment process, due to the need to heat the pulp in the operation of disintegration with live steam to OO6 C, which causes additional costs in the redistribution process, high consumption of liquid glass, due to the need to create a pH of up to 9.5-10 and above which leads to its deposition on the internal walls of pipelines, pumps and mineral processing equipment.
Claims (2)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU772559229A SU698654A1 (en) | 1977-12-26 | 1977-12-26 | Method of concentrating caolines and clays |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU772559229A SU698654A1 (en) | 1977-12-26 | 1977-12-26 | Method of concentrating caolines and clays |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU698654A1 true SU698654A1 (en) | 1979-11-25 |
Family
ID=20739852
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU772559229A SU698654A1 (en) | 1977-12-26 | 1977-12-26 | Method of concentrating caolines and clays |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU698654A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5055204A (en) * | 1989-08-29 | 1991-10-08 | Bogart John D | Soil and sludge treatment apparatus and method including agitation, aeration and recirculation |
-
1977
- 1977-12-26 SU SU772559229A patent/SU698654A1/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5055204A (en) * | 1989-08-29 | 1991-10-08 | Bogart John D | Soil and sludge treatment apparatus and method including agitation, aeration and recirculation |
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