EP1458650A1 - Verfahren zur herstellung von glas und zusammensetzungen dafür - Google Patents
Verfahren zur herstellung von glas und zusammensetzungen dafürInfo
- Publication number
- EP1458650A1 EP1458650A1 EP01985108A EP01985108A EP1458650A1 EP 1458650 A1 EP1458650 A1 EP 1458650A1 EP 01985108 A EP01985108 A EP 01985108A EP 01985108 A EP01985108 A EP 01985108A EP 1458650 A1 EP1458650 A1 EP 1458650A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- glass
- solid state
- state particle
- agglomerate
- calcium
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C03—GLASS; MINERAL OR SLAG WOOL
- C03C—CHEMICAL COMPOSITION OF GLASSES, GLAZES OR VITREOUS ENAMELS; SURFACE TREATMENT OF GLASS; SURFACE TREATMENT OF FIBRES OR FILAMENTS MADE FROM GLASS, MINERALS OR SLAGS; JOINING GLASS TO GLASS OR OTHER MATERIALS
- C03C1/00—Ingredients generally applicable to manufacture of glasses, glazes, or vitreous enamels
- C03C1/02—Pretreated ingredients
- C03C1/026—Pelletisation or prereacting of powdered raw materials
Definitions
- the present invention relates to a product, a process for its preparation, and the use of such
- the present invention relates to a process that produces a
- solid state particle that is particularly useful in the production of glass products, such as flat
- the glass reaction generally involves the reaction of materials to produce a
- composition containing the reacted and/or dispersed components of silica (silicon dioxide from
- Such considerations include, for example, reaction of a portion of the materials before creating a total glass batch.
- one scheme is pretreatment of the batch constituents by calcining the limestone and/or dolomite
- melting begins is advantageous since it reduces the entrapping of gaseous inclusions in the glass.
- thermodynamics or quality or yield results. While advances have been made, there still exists the
- silicates prior to melting is disclosed in which a lowered reaction temperature between
- silica is reacted with sodium carbonate to form sodium silicate in as a
- the method preferably calcines calcium carbonate-
- the present invention discloses a process that includes preferentially reacting a portion of a glass
- the present invention further discloses a solid state particle comprising silicon, calcium and
- the present invention further discloses a glass composition comprising silica, soda ash, lime or
- limestone a solid state particle containing silicon dioxide, calcium hydroxide, magnesium oxide,
- the solid state particle of the present invention is particularly useful in production of glass
- product such as flat glass, fiberglass, container glass, lighting glass, tableware, and the like.
- Figure 1 shows the unreacted silica (stones) per pound of glass as a function of dwell time at a
- the glass batch using the invention will melt faster allowing for more throughput on
- Figure 2 shows the energy evolved or absorbed as a function of temperature for a control glass
- Solid state particle refers to a mixture of
- the solid state particle comprising
- This solid state particle is admixed with a mass containing a balance of other glass-
- Such other glass-forming materials may include
- the silicon material of the solid state particle is silicon dioxide, and, more preferably, a silica
- Preferred sources of such include sand, silica flour, nepheline syenite, and spodumene.
- the silicon material particle size is 90% less than 0.0075 Centimeters to promote a
- thermodynamic advantage towards the solid state reaction versus the standard glass reaction thermodynamic advantage towards the solid state reaction versus the standard glass reaction.
- the calcium material of the solid state particle is calcium oxide and, more preferably, a calcium
- Preferred sources of such include dolomite lime, dolomitic limestone, calcite, lime,
- the calcium material particle size is 90% less than 0.0075 Centimeters to promote a
- thermodynamic advantage towards the solid state reaction versus the standard glass reaction thermodynamic advantage towards the solid state reaction versus the standard glass reaction.
- the magnesium material of the solid state particle is magnesium oxide and, more preferably, a
- magnesium hydroxide Preferred sources of such include dolomitic lime, dolomitic limestone,
- magnesium material particle Preferably the magnesium material particle
- the solid state particle size should be of a magnitude that promotes the attainment and retention
- the solid state particle size should be of a similar magnitude of the other glass batch
- components more preferably of the silicon source material, e. g. sand, used in the total glass
- the median size of the solid state particle material should be from about 75
- a preferred solid state particle material is an agglomerate of minerals produced by the admixture
- agglomerate is formed to a particle size which approximates the sand balance to be used in the glass batch, preferably from about 0.018 centimeters to about 0.14 centimeters, more preferably,
- the product of the reacted solid state particle, that occurs within the total glass batch can be a
- calcium magnesium silicate having an empirical formula of (CaO) x (MgO) y (SiO 2 ) z , wherein the
- weight values of x and y relative to the amount of silica is sufficient to produce an exothermic
- x, y, and z have the respective ranges from about zero (0) to about three (3),
- reaction to completion is provided to the glass batch system.
- a glass product is to have components of silicon, sodium, calcium, magnesium, measurable in
- silica dioxide Si 2
- sodium oxide Na ⁇
- calcium oxide CaO
- magnesium magnesium
- a sand material is selected as a feed material.
- the sand has a size measurement of 30 mesh to 140 mesh.
- silica, and calcium components agglomerated with water, dried, and screened, is added to the
- the agglomerated (solid state) particles contain silicon dioxide (SiO,),
- hydrated calcium oxide Ca(OH) 2
- hydrated magnesium oxide Mg(OH) 2
- periclase MgO
- This agglomerated particle material is combined with the sand to be used in an amount to
- the agglomerated particle does not contain sufficient calcium value for the glass. Since the agglomerated particle does not contain sufficient calcium value for the glass.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Geochemistry & Mineralogy (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Glass Melting And Manufacturing (AREA)
- Glass Compositions (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/US2001/049926 WO2003057636A1 (en) | 2001-12-27 | 2001-12-27 | Method of manufacturing glass and compositions therefore |
Publications (1)
Publication Number | Publication Date |
---|---|
EP1458650A1 true EP1458650A1 (de) | 2004-09-22 |
Family
ID=21743156
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP01985108A Withdrawn EP1458650A1 (de) | 2001-12-27 | 2001-12-27 | Verfahren zur herstellung von glas und zusammensetzungen dafür |
Country Status (9)
Country | Link |
---|---|
EP (1) | EP1458650A1 (de) |
JP (1) | JP4219816B2 (de) |
CN (1) | CN1307115C (de) |
AU (1) | AU2002234091A1 (de) |
BR (1) | BR0117185A (de) |
CA (1) | CA2467176A1 (de) |
HK (1) | HK1070346A1 (de) |
MX (1) | MXPA04005800A (de) |
WO (1) | WO2003057636A1 (de) |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2888243B1 (fr) * | 2005-07-06 | 2007-09-14 | Michelin Soc Tech | Composition de caoutchouc pour pneumatique renforcee de plaquettes d'hydroxyde de magnesium. |
US20070199350A1 (en) * | 2006-02-24 | 2007-08-30 | Butts Dennis I | Methods for producing glass compositions |
EP2437876B1 (de) * | 2009-06-03 | 2018-01-17 | AGC Glass Europe | Verfahren zur herstellung von granulat aus pulvermaterialen |
US9051199B2 (en) * | 2011-02-24 | 2015-06-09 | Owens-Brockway Glass Container Inc. | Process for melting and refining soda-lime glass |
EP2821374A4 (de) | 2012-02-28 | 2015-10-21 | Asahi Glass Co Ltd | Granulierte körper und verfahren zu ihrer herstellung |
CN103408224A (zh) * | 2013-07-30 | 2013-11-27 | 大连尚艺玻璃集团有限公司 | 一种低温电熔明料玻璃配方、工艺方法及制得的明料玻璃 |
JP6332612B2 (ja) * | 2014-03-28 | 2018-05-30 | 日本電気硝子株式会社 | 無アルカリガラスの製造方法 |
WO2017047552A1 (ja) * | 2015-09-17 | 2017-03-23 | 旭硝子株式会社 | ガラス原料造粒体の製造方法、溶融ガラスの製造方法、およびガラス物品の製造方法 |
FR3066810B1 (fr) | 2017-05-23 | 2019-06-14 | Arc France | Four combine |
FR3068347B1 (fr) | 2017-06-30 | 2020-08-28 | Arc France | Preparation de fabrication de verre et four de verrerie |
FR3141458A1 (fr) * | 2022-10-28 | 2024-05-03 | Saint-Gobain Glass France | Procede de fabrication de verre flotte a partir d’un melange de matieres minerales comprenant un silicate de calcium |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE571067A (de) | 1957-09-10 | |||
GB1173777A (en) | 1965-12-27 | 1969-12-10 | Saint Gobain | Pretreated Batch Material for making Glass and other Silicates, and a Process and Apparatus for its Manufacture |
FR1477690A (fr) | 1966-03-09 | 1967-04-21 | Saint Gobain | Procédé de préparation de matière première pour la fabrication du verre |
US3802901A (en) | 1972-09-05 | 1974-04-09 | Fmc Corp | Method of forming granular alkaline earth carbonates |
US4248615A (en) | 1979-11-19 | 1981-02-03 | Owens-Corning Fiberglas Corporation | Pollution abating, energy conserving glass manufacturing process |
US4539030A (en) | 1983-08-03 | 1985-09-03 | Ppg Industries, Inc. | Method of calcining and liquefying glass batch |
GB8728892D0 (en) | 1987-12-10 | 1988-01-27 | Pilkington Plc | Producing molten glass |
US4920080A (en) | 1988-08-19 | 1990-04-24 | Ppg Industries, Inc. | Method of making glass with preliminary reaction of batch materials |
IL121641A0 (en) * | 1996-09-03 | 1998-02-08 | Minerals Tech Inc | Method of producing synthetic silicates and use thereof in glass production |
US6287378B1 (en) * | 1996-09-03 | 2001-09-11 | Minerals Technologies, Inc. | Method of producing synthetic silicates and use thereof in glass production |
US6806244B1 (en) * | 1998-07-29 | 2004-10-19 | Reckitt Benckiser N.V. | Composition for use in water reservoir |
US6358870B1 (en) * | 1999-05-03 | 2002-03-19 | Vitro Corporativo, S.A. De C.V. | Method for preparing pre-reacted batches of raw materials for the production of glass formulas |
US6211103B1 (en) * | 1999-10-12 | 2001-04-03 | Minerals Technologies Inc. | Synthetic silicate pellet compositions |
-
2001
- 2001-12-27 CN CNB018237843A patent/CN1307115C/zh not_active Expired - Lifetime
- 2001-12-27 EP EP01985108A patent/EP1458650A1/de not_active Withdrawn
- 2001-12-27 WO PCT/US2001/049926 patent/WO2003057636A1/en active Application Filing
- 2001-12-27 AU AU2002234091A patent/AU2002234091A1/en not_active Abandoned
- 2001-12-27 JP JP2003557957A patent/JP4219816B2/ja not_active Expired - Fee Related
- 2001-12-27 MX MXPA04005800A patent/MXPA04005800A/es unknown
- 2001-12-27 BR BR0117185-2A patent/BR0117185A/pt not_active Application Discontinuation
- 2001-12-27 CA CA002467176A patent/CA2467176A1/en not_active Abandoned
-
2005
- 2005-04-08 HK HK05102973A patent/HK1070346A1/xx not_active IP Right Cessation
Non-Patent Citations (1)
Title |
---|
See references of WO03057636A1 * |
Also Published As
Publication number | Publication date |
---|---|
JP4219816B2 (ja) | 2009-02-04 |
WO2003057636A1 (en) | 2003-07-17 |
JP2005514308A (ja) | 2005-05-19 |
CN1307115C (zh) | 2007-03-28 |
HK1070346A1 (en) | 2005-06-17 |
BR0117185A (pt) | 2004-11-09 |
MXPA04005800A (es) | 2004-09-10 |
CA2467176A1 (en) | 2003-07-17 |
AU2002234091A1 (en) | 2003-07-24 |
CN1558874A (zh) | 2004-12-29 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20040525 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE TR |
|
AX | Request for extension of the european patent |
Extension state: AL LT LV MK RO SI |
|
RAP1 | Party data changed (applicant data changed or rights of an application transferred) |
Owner name: SPECIALTY MINERALS (MICHIGAN) INC. |
|
17Q | First examination report despatched |
Effective date: 20050118 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
18D | Application deemed to be withdrawn |
Effective date: 20090428 |