SU1611908A1 - Method of producing titanium-calcium pigment - Google Patents
Method of producing titanium-calcium pigment Download PDFInfo
- Publication number
- SU1611908A1 SU1611908A1 SU894655659A SU4655659A SU1611908A1 SU 1611908 A1 SU1611908 A1 SU 1611908A1 SU 894655659 A SU894655659 A SU 894655659A SU 4655659 A SU4655659 A SU 4655659A SU 1611908 A1 SU1611908 A1 SU 1611908A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- pigment
- amount
- product
- titanium
- calcined
- Prior art date
Links
- 239000000049 pigment Substances 0.000 title claims abstract description 12
- 238000000034 method Methods 0.000 title claims abstract description 6
- JTCFNJXQEFODHE-UHFFFAOYSA-N [Ca].[Ti] Chemical compound [Ca].[Ti] JTCFNJXQEFODHE-UHFFFAOYSA-N 0.000 title claims description 3
- 239000004115 Sodium Silicate Substances 0.000 claims abstract description 7
- 239000000292 calcium oxide Substances 0.000 claims abstract description 7
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims abstract description 7
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052911 sodium silicate Inorganic materials 0.000 claims abstract description 7
- 238000001354 calcination Methods 0.000 claims abstract description 5
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims abstract description 5
- HDUMBHAAKGUHAR-UHFFFAOYSA-J titanium(4+);disulfate Chemical compound [Ti+4].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O HDUMBHAAKGUHAR-UHFFFAOYSA-J 0.000 claims abstract description 5
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims abstract description 3
- 150000003608 titanium Chemical class 0.000 claims abstract 2
- 239000000203 mixture Substances 0.000 claims description 8
- 238000000227 grinding Methods 0.000 claims description 6
- 229940072033 potash Drugs 0.000 claims description 4
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 claims description 4
- 235000015320 potassium carbonate Nutrition 0.000 claims description 4
- 239000002253 acid Substances 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims 1
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims 1
- 239000011575 calcium Substances 0.000 claims 1
- 229910052791 calcium Inorganic materials 0.000 claims 1
- 239000001023 inorganic pigment Substances 0.000 abstract description 2
- 238000002360 preparation method Methods 0.000 abstract description 2
- 239000000126 substance Substances 0.000 abstract description 2
- 230000002378 acidificating effect Effects 0.000 abstract 1
- 239000000047 product Substances 0.000 description 8
- BUACSMWVFUNQET-UHFFFAOYSA-H dialuminum;trisulfate;hydrate Chemical compound O.[Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O BUACSMWVFUNQET-UHFFFAOYSA-H 0.000 description 4
- 239000002244 precipitate Substances 0.000 description 3
- 239000000725 suspension Substances 0.000 description 3
- 238000001238 wet grinding Methods 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- RSXAMZBVVFHQJX-UHFFFAOYSA-J S(=O)(=O)([O-])[O-].[Ti+4].S(=O)(=O)([O-])[O-].[Ti+4] Chemical compound S(=O)(=O)([O-])[O-].[Ti+4].S(=O)(=O)([O-])[O-].[Ti+4] RSXAMZBVVFHQJX-UHFFFAOYSA-J 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000004061 bleaching Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- VCSZKSHWUBFOOE-UHFFFAOYSA-N dioxidanium;sulfate Chemical compound O.O.OS(O)(=O)=O VCSZKSHWUBFOOE-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 229910021653 sulphate ion Inorganic materials 0.000 description 1
- 230000004083 survival effect Effects 0.000 description 1
- 229910052719 titanium Inorganic materials 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- 229910000349 titanium oxysulfate Inorganic materials 0.000 description 1
- -1 titanium salt Chemical class 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/0081—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound
- C09C1/0084—Composite particulate pigments or fillers, i.e. containing at least two solid phases, except those consisting of coated particles of one compound containing titanium dioxide
Landscapes
- Chemical & Material Sciences (AREA)
- Composite Materials (AREA)
- Organic Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
Abstract
Изобретение относитс к химической технологии, в частности к получению неорганических пигментов. Цель изобретени состоит в повышении белизны и диспергируемости пигмента при сокращении продолжительности процесса. Поставленна цель достигаетс тем, что сернокислую титановую соль смешивают к активным оксидом кальци , вз тым в 1,5-3,5%-ном избытке к стехиометрическому количеству его по отношению к SO3 - кислому в титановой соли. Полученный продукт прокаливают и измедьчение прокаленного продукта ведут с добавкой силиката натри в количестве 0,05-0,25% SIO2 и сульфата алюмини в количество 0,3-0,8 AL2O3 по отношению к весу продукта.This invention relates to chemical technology, in particular to the preparation of inorganic pigments. The purpose of the invention is to increase the whiteness and dispersibility of the pigment while reducing the duration of the process. The goal is achieved by the fact that the titanium sulfate salt is mixed to active calcium oxide, taken in a 1.5-3.5% excess of its stoichiometric amount relative to SO 3 - acidic in the titanium salt. The resulting product is calcined and the calcination of the calcined product is carried out with the addition of sodium silicate in an amount of 0.05-0.25% SIO 2 and aluminum sulfate in an amount of 0.3-0.8 AL 2 O 3 in relation to the weight of the product.
Description
Изобретение относитс к химической технологии, в частности к получению неорганических пигментов, используемых в производстве лакокрасочных материалов, бумаги, пластмасс.The invention relates to chemical technology, in particular to the preparation of inorganic pigments used in the manufacture of paints, paper, plastics.
Цель изобретени - повьшение бе- лизны и диспергируемости пигмента при с окращении пpoдQлжитeльнocти процесса .The purpose of the invention is to increase the purity and dispersibility of the pigment with the reduction of the survival rate of the process.
Пример 1. 1 кг сернокислой титановой соли (сульфат титаниламмо- ни ) смешивают с 155 г активного оксида кальци (3,5%-ньй избыток от стехиометрического количества к SOj- кислому в титановой соли) и 1 г минерализатора - поташа. Смесь прокаливают при 650-700°С в течение. 2, 5 ч. Прокаленный продукт подвергают мокрому измельчению с добавкой силиката натри в количестве 0,05% ., аExample 1. 1 kg of titanium sulfate salt (titanylammonium sulfate) is mixed with 155 g of active calcium oxide (3.5% excess from stoichiometric amount to SOj-acidic in titanium salt) and 1 g of mineralizer - potash. The mixture is calcined at 650-700 ° C for. 2, 5 h. The calcined product is subjected to wet grinding with the addition of sodium silicate in an amount of 0.05%., And
затем (через 20-30 мин) сульфата алюмини в количестве 0,8% А1„0з по отношению к весу продукта. Обща продолжительность измельчени 2 ч. Сус- пе11зию фильтруют, осадок сушат при 150-180 0. Полученный титанокальцие- вый пигмент (ТКП) (содержание ТЮ 34,0%) обладает следующими мал рно- техническими свойствами (белизна - (Б), разбеливающа способность - (Р), укрьшистость - (у), маслоемкость - (М), диспергируемость - (Д));then (after 20-30 minutes) aluminum sulfate in the amount of 0.8% A1 „0z relative to the weight of the product. The total grinding time is 2 hours. Suspension is filtered, the precipitate is dried at 150-180 0. The resulting titanium-calcium pigment (TKP) (TU content 34.0%) has the following small p-technical properties (whiteness - (B), ability - (P), ukrshistosti - (y), oil absorption - (M), dispersibility - (D));
Б, усл.ед.B, used
Р, усл.ед.P, used
У, г/мY, g / m
М, г/100 г пигментаM, g / 100 g of pigment
Д, мкмD, micron
96,096.0
450450
69,569.5
26,026.0
5050
эоeo
Пример 2. 1кг сернокислой титановой соли (титанилсульфат дигид- рат) смешивают со 183,4 г активногоExample 2. 1 kg of titanium sulfate salt (titanyl sulfate dihydrate) is mixed with 183.4 g of active
316316
оксида кальци ( избыток от стехиометрическогб количества к SOg- |кислому в соли) и 7,3 г минерализатора - 1гюташа. Смесь прокаливают при 650- |700 С в течение 3,0 ч. Прокаленный продукт подвергают мокрому измельче- 1НИЮ с добавкой силиката натри в ко- :личестве 0,15% SiO, а затем (через 120-30 мин) сульфата алюмини в коли- честве 0,53% по отношению к весу продукта. Обща продолжительность измельчени 2 ч. Суспензию фильтруют, осадок сушат при 150-180 С Лолученный ТКП (содержание Т 10,234, 2%) обладает следующими мал рно-техничес- кими свойствами: calcium oxide (excess stoichiometric amount to SOg- | acid in salt) and 7.3 g of mineralizer - 1g. The mixture is calcined at 650- | 700 C for 3.0 hours. The calcined product is subjected to wet grinding with the addition of sodium silicate in a quantity of 0.15% SiO, and then (after 120-30 minutes) aluminum sulphate in - quality 0.53% in relation to the weight of the product. The total grinding time is 2 hours. The suspension is filtered, the precipitate is dried at 150-180 ° C. The obtained TCP (T content 10.234, 2%) has the following low-technical properties:
Б, усл.,ед.95,8B, cond., Unit 95.8
Р, усл.ед. . 470 У, P, used . 470 W,
Ы, г/100 г пигмента 26,8. Д, мкм45N, g / 100 g of pigment 26.8. D, μm45
Пример 3, 1 кг сернокислой титановой соли (безводный титанил- сульфат) смешивают с 354,2 г актив- ного оксида кальци (1,5%-ный избыток от стехиометрического количества к 50--кислому в соли), добавл ют 6 г минерализатора - поташа. Смесь прокаливают при 650-700°С в течение 3,5. ч Прокаленный продукт подвергают мокрому измельчению с добавкой силиката натри в количестве 0,25% SiO, а затем (через 20-30 мин) сульфата алю- в кохшчестве 0,3% по отношению к весу продукта. Обща продолжительность измельчени 2 ч. Суспензию фильтруют, осадок сушат при 150-180°С. Полученный Т1Ш (содержани TiOg 31,5%) обладает следующими ма л рно-техническими свойствами;Example 3, 1 kg of titanium sulphate (anhydrous titanyl sulphate) is mixed with 354.2 g of active calcium oxide (1.5% excess from a stoichiometric amount to 50% acid in salt), 6 g of mineralizer are added - potash. The mixture is calcined at 650-700 ° C for 3.5. The calcined product is subjected to wet grinding with the addition of sodium silicate in an amount of 0.25% SiO, and then (after 20–30 minutes) aluminum sulphate in the amount of 0.3% relative to the weight of the product. The total grinding time is 2 hours. The suspension is filtered, the precipitate is dried at 150-180 ° C. The obtained T1SH (TiOg content 31.5%) has the following metal-technical properties;
Б, усл.ед, Р, усл.ед. У, Г/мB, used, P, used U, G / m
М, г/100 г пигмента мкмM, g / 100 g pigment microns
95,095.0
600600
60,160.1
4040
4040
Д,D,
пример 4 (по известному способу ) . 1 кг сернокислой титановой соли - сульфата титани,ла и аммони , смеишвают со 150 г извести и 2 г (1% к TiO) минерализатора - поташа. Смесь прокаливают при 650-700 С« Пркаленный продукт измельчают. В резултате получают пигментную композицию, содержащую 35,4% двуокиси титана, имщую следующие показатели: example 4 (by a known method). 1 kg of titanium sulfate salt - titanium sulfate, la and ammonium, is mixed with 150 g of lime and 2 g (1% of TiO) of the mineralizer - potash. The mixture is calcined at 650-700 ° C. “The calcined product is crushed. As a result, a pigment composition containing 35.4% of titanium dioxide is obtained, having the following characteristics:
Q Q
00
5five
30thirty
3535
Б,усл.ед.B, used
Р,усл.ед.P, used
М,г/100 г пигментаM, g / 100 g of pigment
У,г/мY, g / m
Д,мкмD, micron
93,493.4
440440
26,326.3
7070
7878
Примеры свидетельствуют о том, . что при осуществлении предлагаемого способа по сравнению с известным достигаютс повышение белизны (на 2-3 усл.ед.), снижение показател диспер- гируемости на 20-35 мкм без ухудшени других пигментных свойств ТКП. Кроме того, сокращаетс продолжительность прокаливани смеси в 2 раза.Examples suggest. that when implementing the proposed method in comparison with the known one, an increase in whiteness is achieved (by 2-3 standard units), a decrease in the dispersibility index by 20-35 µm without deterioration of other pigment properties of TCP. In addition, the calcination time of the mixture is halved.
При добавке в реакционную смесь СаО в избытке 1,5% увеличиваетс продолжительность прокаливани , снижаетс белизна и диспергируемость, избыток СаО 3,5% практически не вли ет на продолжительность прокаливани и белизну ТКП, но приводит к снижению разбеливающей способности и укрывис- тости.When CaO is added to the reaction mixture in an excess of 1.5%, the calcination time increases, whiteness and dispersibility decrease, an excess of CaO 3.5% practically does not affect the calcination time and the whiteness of the SCT, but leads to a decrease in bleaching capacity and opacity.
Добавка при измельчении прокаленного продукта силиката натри в количестве сО, 05% SiO и сульф.ата алюмини :-053% 3 приводит к. снижению белизны и диспергируемости Т1Ш. Расход силиката натри и сульфата алюмини в количестве 0,25% SiO, ,8% практически не вли ет на белизну и диспергируемость ТКП, но снижает его разбеливающую способность и укры- вистость.The additive, when grinding the calcined product of sodium silicate in the amount of CO, 05% SiO and aluminum sulphate: -053% 3 leads to a decrease in whiteness and dispersibility of T1Sh. The consumption of sodium silicate and aluminum sulphate in the amount of 0.25% SiO,, 8% has practically no effect on the whiteness and dispersibility of the TCH, but reduces its whitening ability and hiding power.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU894655659A SU1611908A1 (en) | 1989-02-27 | 1989-02-27 | Method of producing titanium-calcium pigment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SU894655659A SU1611908A1 (en) | 1989-02-27 | 1989-02-27 | Method of producing titanium-calcium pigment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| SU1611908A1 true SU1611908A1 (en) | 1990-12-07 |
Family
ID=21431043
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| SU894655659A SU1611908A1 (en) | 1989-02-27 | 1989-02-27 | Method of producing titanium-calcium pigment |
Country Status (1)
| Country | Link |
|---|---|
| SU (1) | SU1611908A1 (en) |
-
1989
- 1989-02-27 SU SU894655659A patent/SU1611908A1/en active
Non-Patent Citations (1)
| Title |
|---|
| Авторское свидетельство СССР № l l71490, кл; С 09 С 1/36, 1985. * |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| FI101217B (en) | Precipitated calcium carbonate | |
| US4539195A (en) | Basic magnesium aluminum hydroxycarbonate | |
| US3862297A (en) | Manufacture of pigmentary titanium dioxide | |
| RU2171228C2 (en) | Rutile titanium dioxide and methods of preparing thereof (variants) | |
| DE372715T1 (en) | POLYMER BASIC ALUMINUM SILICATE SULFATE. | |
| US5037477A (en) | Process for the preparation of an acid-resistant coating on filler particles | |
| DE2623482C2 (en) | Process for the production of a crystalline aluminum oxide for polishing, lapping and grinding media | |
| US2213168A (en) | Composite pigments and process of making the same | |
| SU1611908A1 (en) | Method of producing titanium-calcium pigment | |
| DE3806187A1 (en) | COMPOSED PHYLLOSILICATE AND METHOD FOR THE PRODUCTION THEREOF | |
| SU865131A3 (en) | Method of producing coloured pigments based on titanium compounds | |
| US3592674A (en) | Method of preparing a calcium carbonate-magnesium hydroxide pigment and the pigment produced | |
| US4702776A (en) | Preparation of pigmentary red iron oxides | |
| DE2852674A1 (en) | METHOD FOR PRODUCING ZEOLITH A FROM KAOLIN | |
| US4049463A (en) | Method for producing a pure cerium oxide | |
| DE2600485A1 (en) | Calcium and magnesium carbonates suitable for paper mfr - made by feeding carbon dioxide into aq suspension of calcined dolomite | |
| US4455284A (en) | Process for desilication of aluminate solution | |
| RU2090501C1 (en) | Method of preparing finely dispersed wollastonite | |
| CA2478670C (en) | Method for the production of precipitated calcium carbonate with a high degree of brightness | |
| KR920008517B1 (en) | Process for separating off barium from water-soluble strontium salts | |
| US2361986A (en) | Composite pigments and process of producing same | |
| RU2096331C1 (en) | Method of sphene concentrate processing | |
| US2170800A (en) | Process for making composite titanium pigments | |
| SU1640136A1 (en) | Method for modification of titanium dioxide pigment | |
| DE1646513C3 (en) | Process for the production of praseodymium- or vanadium-containing zirconium stains |