SU120465A1 - Method for flotation separation of titanium-zirconium products - Google Patents
Method for flotation separation of titanium-zirconium productsInfo
- Publication number
- SU120465A1 SU120465A1 SU585220A SU585220A SU120465A1 SU 120465 A1 SU120465 A1 SU 120465A1 SU 585220 A SU585220 A SU 585220A SU 585220 A SU585220 A SU 585220A SU 120465 A1 SU120465 A1 SU 120465A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- titanium
- flotation separation
- zirconium products
- zirconium
- flotation
- Prior art date
Links
- 238000000034 method Methods 0.000 title description 7
- 238000005188 flotation Methods 0.000 title description 6
- 238000000926 separation method Methods 0.000 title description 6
- PMTRSEDNJGMXLN-UHFFFAOYSA-N titanium zirconium Chemical compound [Ti].[Zr] PMTRSEDNJGMXLN-UHFFFAOYSA-N 0.000 title description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 229910052845 zircon Inorganic materials 0.000 description 4
- GFQYVLUOOAAOGM-UHFFFAOYSA-N zirconium(iv) silicate Chemical compound [Zr+4].[O-][Si]([O-])([O-])[O-] GFQYVLUOOAAOGM-UHFFFAOYSA-N 0.000 description 4
- 229910001773 titanium mineral Inorganic materials 0.000 description 3
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 description 1
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 description 1
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 description 1
- 239000005642 Oleic acid Substances 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 description 1
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 description 1
- 238000010926 purge Methods 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
Landscapes
- Manufacture And Refinement Of Metals (AREA)
Description
Известны способы флотационного разделени титано-циркониевых продуктов. Однако процесс селективной флотации титановых минералов от циркона, управл емый газами, до насто щего времени не был известен .Methods for flotation separation of titanium-zirconium products are known. However, the process of selective flotation of titanium minerals from gas-controlled zircon was not known until now.
В описываемом способе предлагаетс обрабатывать (продувать) исходную пульпу азотом с последующим выделением циркона в пенный продукт. При такой обработке азот депрессирует титановые минералы, не оказыва в то же врем вли ни на флотационную активность циркона , который легко переходит в пенный продукт, а титан остаетс в хвостах.In the described method, it is proposed to process (purge) the original pulp with nitrogen followed by separation of the zircon into the froth product. In this treatment, nitrogen depresses titanium minerals, without at the same time affecting the flotation activity of zircon, which easily passes into the froth product, and titanium remains in the tails.
При использовании предлагаемого способа расход олеиновой кислоты при флотации составл ет 700 г/т и соды 400 г/т врем предварительной обработки пульпы азотом - 40-50 мин.When using the proposed method, the oleic acid consumption during flotation is 700 g / t and soda 400 g / t. The pretreatment time of the pulp with nitrogen is 40-50 minutes.
Предмет изобретени Subject invention
Способ флотационного разделени титано-циркониевых продуктов, отличающийс тем, что, с целью повышени эффективности разделени , исходную пульпу обрабатывают (.продувают) азотом с последующим выделением циркона в пенный продукт при депрессии титановых минералов.A method of flotation separation of titanium-zirconium products, characterized in that, in order to increase the separation efficiency, the original pulp is treated (.produced) with nitrogen, followed by separation of zircon into the froth product during depression of titanium minerals.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU585220A SU120465A1 (en) | 1957-10-28 | 1957-10-28 | Method for flotation separation of titanium-zirconium products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU585220A SU120465A1 (en) | 1957-10-28 | 1957-10-28 | Method for flotation separation of titanium-zirconium products |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU120465A1 true SU120465A1 (en) | 1958-11-30 |
Family
ID=48392334
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU585220A SU120465A1 (en) | 1957-10-28 | 1957-10-28 | Method for flotation separation of titanium-zirconium products |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU120465A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3669266A (en) * | 1969-09-15 | 1972-06-13 | Ethyl Corp | Minerals separation process |
-
1957
- 1957-10-28 SU SU585220A patent/SU120465A1/en active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3669266A (en) * | 1969-09-15 | 1972-06-13 | Ethyl Corp | Minerals separation process |
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