YU200090A - PROCEDURE FOR OBTAINING SODIUM SILICATE - Google Patents
PROCEDURE FOR OBTAINING SODIUM SILICATEInfo
- Publication number
- YU200090A YU200090A YU200090A YU200090A YU200090A YU 200090 A YU200090 A YU 200090A YU 200090 A YU200090 A YU 200090A YU 200090 A YU200090 A YU 200090A YU 200090 A YU200090 A YU 200090A
- Authority
- YU
- Yugoslavia
- Prior art keywords
- sodium silicate
- temperature
- sio2
- molar ratio
- powdered
- Prior art date
Links
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
POSTUPAK ZA DOBIJANJE NATRIJUM SILIKATA, amorfni natrijum silikat sa 0,3 do 6 mas. % vode i molskim odnosom izmedju SiO2 i Na2O (1,9 do 2,8) : 1 se dobija iz rastopa stakla sa najmanje 20% mas. čvrstih materija, što se rastopina stakla i natrijumhidroksida sa molskim odnosom SiO2 : NaO (2,0 do 2,8) : 1 tretira na temperaturi od 180В°C-240В°C i pritisku od 10-30 v. Tu rastopinu izložimo u zoni sušenja sa vazduhom na temperaturi 200-300В°C 10-20s, zatim na temperaturi 90-130В°C pri čemu nastaje praškasti amorfni natrijumsilikat sa sadržajem vode (dodate pri žarenju na 700В°C) 15 do 23 mas.% i nasipnom masom od 300 g/l. Praškasti natrijev silikat se dalje tretira u koso postavljenoj aparaturi za pomeranje čvrstih materija tj. u rotacionoj cevnoj peći kroz koju prolaze dimni gasovi na temperaturi u 250-500 В°C u vremenu od 1. 60 min. Temperatura spoljneg zida rotacione peći je oko 60В°C. Dobijeni amorfni natrijum silikat se drobi pomoću mehaničke drobilice na zrna od 0,1-12 mm.PROCESS FOR OBTAINING SODIUM SILICATE, amorphous sodium silicate with 0.3 to 6 wt. % of water and the molar ratio between SiO2 and Na2O (1.9 to 2.8): 1 is obtained from a glass melt with at least 20% by weight. solids, which are a solution of glass and sodium hydroxide with a molar ratio of SiO2: NaO (2.0 to 2.8): 1 is treated at a temperature of 180V ° C-240V ° C and a pressure of 10-30 C. This solution is exposed in an air-drying zone at a temperature of 200-300V ° C for 10-20 s, then at a temperature of 90-130V ° C, whereby powdered amorphous sodium silicate with a water content (added during annealing at 700V ° C) of 15 to 23 wt. % and bulk density of 300 g / l. Powdered sodium silicate is further treated in an obliquely placed apparatus for moving solids, i. in a rotary tube furnace through which flue gases pass at a temperature of 250-500 V ° C for a period of 1. 60 min. The temperature of the outer wall of the rotary kiln is about 60V ° C. The obtained amorphous sodium silicate is crushed by means of a mechanical crusher into grains of 0.1-12 mm.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SI9012000A SI9012000A (en) | 1989-10-25 | 1990-10-24 | Method for preparation of sodium silicates |
HRP-2000/90A HRP921199B1 (en) | 1989-10-25 | 1992-11-06 | A process for the preparation of natrium silicates |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3935464 | 1989-10-25 |
Publications (1)
Publication Number | Publication Date |
---|---|
YU200090A true YU200090A (en) | 1994-09-09 |
Family
ID=47470738
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
YU200190A YU200190A (en) | 1989-10-25 | 1990-10-02 | PROCEDURE FOR OBTAINING SODIUM SILICATE |
YU200090A YU200090A (en) | 1989-10-25 | 1990-10-24 | PROCEDURE FOR OBTAINING SODIUM SILICATE |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
YU200190A YU200190A (en) | 1989-10-25 | 1990-10-02 | PROCEDURE FOR OBTAINING SODIUM SILICATE |
Country Status (1)
Country | Link |
---|---|
YU (2) | YU200190A (en) |
-
1990
- 1990-10-02 YU YU200190A patent/YU200190A/en unknown
- 1990-10-24 YU YU200090A patent/YU200090A/en unknown
Also Published As
Publication number | Publication date |
---|---|
YU200190A (en) | 1994-09-09 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AR247369A1 (en) | Method for preparation of sodium silicates | |
ES2047898T3 (en) | PROCEDURE FOR OBTAINING SODIC SILICATES. | |
BR9200764A (en) | PROCESS FOR THE PREPARATION OF SODIUM SILICATES | |
RO120063B1 (en) | Process for neutralizing inert ash | |
ES2073778T3 (en) | PROCEDURE FOR THE HYDROTHERMAL OBTAINING OF CRYSTALLINE SODIUM DISILICATE. | |
JPH07102977B2 (en) | Waste treatment method and equipment | |
YU200090A (en) | PROCEDURE FOR OBTAINING SODIUM SILICATE | |
JP2010111561A (en) | Method for producing artificial zeolite using waste glass as raw material | |
JPS5462654A (en) | Method of treating waste water containing heavy metal | |
DE3269075D1 (en) | Process for making foam-glass products | |
GB1527155A (en) | Preparing alkali metal silicate glass | |
CN115138668B (en) | Fly ash treatment method | |
RU2058030C1 (en) | Method for determination of difficulty hydrated free cao being covered by glass phase in brown ash | |
JP4409102B2 (en) | Heavy metal elution reducing material | |
SU105858A1 (en) | Method for determination of loparite mineral content in loparite concentrates | |
BR102018067509A2 (en) | POZOLAN MANUFACTURING PROCESS FROM BAUXITE WASTE AND BAUXITE WASTE POZOLAN | |
JP4428613B2 (en) | Exhaust gas treatment material, gas filter, and exhaust gas treatment method using them | |
SU775075A1 (en) | Binder | |
JPS55141512A (en) | Covering and heat insulating material for molten metal | |
GB1099773A (en) | Process for the production of steam hardened cemented products from waste products of the soda industry | |
JPS55121875A (en) | Method and apparatus for treating waste material | |
Shen et al. | THEORETICAL BASIS AND STATE-OF-ART OF STUDY ON THE IMMOBILISATION OF RADIOACTIVE WASTE BY MEANS OF CEMENT AND SOME CONSIDERATIONS FOR THE RESEARCH OF CEMENT CHEMISTRY | |
Osborn et al. | Chemical reactions of fly ash from refuse incineration | |
GB1069228A (en) | Improvements in or relating to the refining of glass | |
JPS51146394A (en) | The manufacturing process and apparatus for sodium silicate |