WO2007105029A1 - A process for the production of reactive blast furnace slag - Google Patents
A process for the production of reactive blast furnace slag Download PDFInfo
- Publication number
- WO2007105029A1 WO2007105029A1 PCT/IB2006/002077 IB2006002077W WO2007105029A1 WO 2007105029 A1 WO2007105029 A1 WO 2007105029A1 IB 2006002077 W IB2006002077 W IB 2006002077W WO 2007105029 A1 WO2007105029 A1 WO 2007105029A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- slag
- blast furnace
- furnace slag
- reactive
- range
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B18/04—Waste materials; Refuse
- C04B18/14—Waste materials; Refuse from metallurgical processes
- C04B18/141—Slags
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B18/04—Waste materials; Refuse
- C04B18/14—Waste materials; Refuse from metallurgical processes
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B18/04—Waste materials; Refuse
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y99/00—Subject matter not provided for in other groups of this subclass
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Definitions
- the present invention relates to a process for the production of reactive granulated blast furnace slag.
- the invention particularly relates to a process for increasing the reactivity of ground granulated blast furnace slag using surface activation through mechanical activation in high energy mills that exploit large contact area between milling media and the material.
- the products produced by the process of present invention may be of different particle sizes and shapes, different specific surface areas, different surface charge (Zeta potential) and different reactivity.
- the reactive blast furnace slag shall be useful in Portland Slag Cement (PSC) 5 Geopolymer, immobilisation and stabilisation of toxic wastes and newer nano-composite materials.
- the blast furnace slag has latent hydraulic activity, i.e. develops cementitious properties when exposed to water.
- the reactivity of blast furnace slag is defined in terms of rate at which it hydrates and forms the hydration product in water. Water is present in the slag hydration product in evaporable and non-evaporable forms. Higher amount of non- evaporable water signifies greater hydration. If the two slag samples are hydrated under identical condition, then the one that shows higher amount of non-evaporable water will have greater reactivity.
- WO2004/041746 Al 2004, Process for producing blended cement with reduced carbon dioxide emissions, by Vladimir Ronin, wherein the reactivity of the blast furnace slag was improved by dry grinding to a specific surface area of 1000 cm 2 /g in the first step and 3000 cm 2 /g in the final step.
- the hitherto known process to increase the reactivity of the blast furnace slag without any chemical addition is based on prolonged grinding in a conventional mill device such as ball mill, rod mill etc.
- the hydration of blast furnace slag takes few months to years. c. The slag does not form any crystalline product during hydration reactions. d. The production cost of slag is relatively high as it uses prolonged grinding and consumes energy. e. Due to slow hydration rate, the use of slag, e.g. in Portland slag cement, is restricted.
- the main object of the present investigation is to provide a process for the production of reactive blast furnace slag, which obviates the drawbacks as detailed above.
- Another object of the present invention is to provide an improved process to produce reactive blast furnace slag whereby the energy consumption is significantly reduced.
- Yet another object of the present invention is to provide an improved process to produce reactive blast furnace slag whereby the reactivity of the slag significantly enhanced.
- the present invention particularly provides a process for increasing the reactivity of ground granulated blast furnace slag using surface activation through short mechanical activation time (10-60 min) and it starts to hydrate in short time (48 h or less) when mixed with water without any chemical additive and completely hydrates in maximum 28 days forming cementitious product.
- the products produced by the process of present invention may be of different particle sizes and shapes, different specific surface areas, different surface charge (Zeta potential) and different reactivity.
- the reactive blast furnace slag shall be useful in Portland Slag Cement (PSC), Geopolymer, immobilisation and stabilisation of toxic wastes and newer nano-composite materials.
- the granulated blast furnace slag used in the present invention contains calcium oxide (CaO), silica (SiO 2 ), alumina (Al 2 O 3 ) and magnesium oxide (MgO) and it is mostly glassy in nature.
- the blast furnace slag does not actively participate in the hydration reaction; as a result it hydrates very slowly and incompletely.
- the blast furnace slag is wet milled in water using a high-energy mill to mechanically activate the slag.
- the mill is characterised by small media size ( ⁇ 10 mm) and an agitator that rotates the media at high rpm (> 250 rpm) resulting in high kinetic energy and large contact between the material and the grinding media.
- the mill is referred to as an attrition mill or agitator bead mill or stirred media mill (the term attrition mill is used in all subsequent description).
- the milling process mechanically activates the granulated blast furnace slag and its reactivity is increased.
- the process of mechanical activation results due to breakage of slag to very fine size and other physicochemical changes, in particular surface changes or surface activation.
- the increased reactivity of blast furnace slag results from the destabilisation of impervious aluminosilicate surface film that is responsible for retardation/inhibition of slag hydration in the case of conventionally milled slag.
- the increased reactivity leads to enhanced hydraulic activity of slag.
- the reactive blast furnace slag can begin to hydrates in 24-48 hours even if no chemical activator is present. Complete hydration can be achieved in less than 28 days.
- the nature of hydration product and its crystallinity is changed through the variation of parameters during mechanical activation process.
- the present invention provides a process for the production of reactive blast furnace slag, which comprises:
- the granulated blast furnace slag used has the following composition range: SiO 2 - 20 to 40%, Al 2 O 3 - 20 to 40%, Fe 2 O 3 - 0 to 2%, CaO - 20 to 40%, MgO - 5 to 17%, MnO - 0 to 5%, SO 3 - 0 to 2% and glass content >85%.
- the blast furnace slag may be selected from the following composition range: Constituent Granulated blast furnace slag
- the reactive : blast furnace slag obtained in the present invention may have the following range of properties:
- Phases after hydration time Amorphous to mostly crystalline phases depending upon properties (a)-
- Novelty of the present invention is that the reactivity of the slag is significantly improved in short mechanical activation time (10-60 min) and it start to hydrate in short time (48 h or less) when mixed with water without any chemical additive and completely hydrates in maximum 28 days forming cementitious product. Also, the hydration phases formed are crystalline in nature. Due to enhanced reactivity the higher proportion of slag is used in products such as Portland slag cement, matrix for immobilisation and stabilisation of toxic wastes, geopolymers and nano-composites.
- 1 kg of the blast furnace slag was dry milled in a ball mill for a period of 45 min.
- the particle size obtained after the ball milling was -100 micron.
- 150 grams of ball milled blast furnace slag was used as a feed material and wet milled in an attrition mill for 10 minutes using water as medium.
- the material to water ratio was kept as 1 :1.5 and material to ball ratio was kept 1 :10.
- the size of the ball was 2 mm and agitator speed was 1000 rpm.
- the attrition milled slag was evaluated in terms of median particle size, morphology, Zeta potential, stable suspension volume (volume occupied by 100 g slag when excess water is present), hydration start time.
- Standard isothermal conduction calorimetric procedure was employed to find hydration start time.
- Slag slurry from the mill equivalent to 100 g of slag, was allowed to hydrate for 28 days at room temperature.
- Reactivity of the slag was measured using a 28 day hydrated neat slag sample and expressed in terms of thermogravimetric weight loss in the temperature range 105-950 0 C per gram of hydrated slag or slag taken for hydration.
- the hydration product was also evaluated in terms of its microstructural characteristic and phases present and their crystallinity.
- the properties of the reactive blast furnace slag obtained are furnished in table 1.
- 1 kg of the blast furnace slag was dry milled in a ball mill for a period of 45 min.
- the particle size obtained after the ball milling was -100 micron.
- 150 grams of ball milled blast furnace slag was used as a feed material and wet milled in an attrition mill for 15 minutes using water as medium.
- the material to water ratio was kept as 1:1.5 and material to ball ratio was kept 1:10.
- the size of the ball was 2 mm and agitator speed was 1000 rpm.
- the attrition milled slag was evaluated in terms of median particle size, morphology, Zeta potential, stable suspension volume (volume occupied by 100 g slag when excess water is present), hydration start time.
- Standard isothermal conduction calorimetric procedure was employed to find hydration start time.
- the water present in attrition milled slurry was separated by filtering and then the material was dried at 40 0 C in an electric oven for 6 hours and then cooled to room temperature.
- 100 g of the dried slag was mixed with excess water such that it was completely immersed in water, and allowed to hydrate for 28 days at room temperature.
- Reactivity of the slag was measured using a 28 day hydrated neat slag sample and expressed in terms of thermogravirnetric weight loss in the temperature range 105-950 0 C per gram of hydrated slag or slag taken for hydration.
- the hydration product was also evaluated in terms of its microstructural characteristic and phases present and their crystallinity.
- the properties of the reactive blast furnace slag obtained are furnished in table 2.
- 1 kg of the blast furnace slag was dry milled in a ball mill for a period of 45 min.
- the particle size obtained after the ball milling was -100 micron.
- 150 grams of ball milled blast furnace slag was used as a feed material and wet milled in an attrition mill for 30 minutes using water as medium.
- the material to water ratio was kept as 1:1.5 and material to ball ratio was kept 1:10.
- the size of the ball was 2 mm and agitator speed was 1000 rpm.
- the attrition milled slag was evaluated in terms of median particle size, morphology, Zeta potential, stable suspension volume (volume occupied by 100 g slag when excess water is present), hydration start time.
- Standard isothermal conduction calorimetric procedure was employed to find hydration start time.
- Slag slurry from the mill equivalent to 100 g of slag, was allowed to hydrate for 28 days at room temperature.
- Reactivity of the slag was measured using a 28 day hydrated neat slag sample and expressed in terms of thermogravimetric weight loss in the temperature range 105-950 0 C per gram of hydrated slag or slag taken for hydration.
- the hydration product was also evaluated in terms of its microstructural characteristic and phases present and their crystallinity.
- the properties of the reactive blast furnace slag obtained are furnished in table 3.
- 1 kg of the blast furnace slag was dry milled in a ball mill for a period of 45 min.
- the particle size obtained after the ball milling was -100 micron.
- 150 grams of ball milled blast furnace slag was used as a feed material and wet milled in an attrition mill for 60 minutes using water as medium.
- the material to water ratio was kept as 1 :1.5 and material to ball ratio was kept 1:10.
- the size of the ball was 2 mm and agitator speed was 1000 rpm.
- the attrition milled slag was evaluated in terms of median particle size, morphology, Zeta potential, stable suspension volume (volume occupied by 100 g slag when excess water is present), hydration start time.
- Standard isothermal conduction calorimetric procedure was employed to find hydration start time.
- Slag slurry from the mill equivalent to 100 g of slag, was allowed to hydrate for 28 days at room temperature.
- Reactivity of the slag was measured using a 28 day hydrated neat slag sample and expressed in terms of thermogravimetric weight loss in the temperature range 105-950 0 C per gram of hydrated slag or slag taken for hydration.
- the hydration product was also evaluated in terms of its microstructural characteristic and phases present and their crystallinity.
- the properties of the reactive blast furnace slag obtained are furnished in table 4.
- the process is fast and energy efficient due to increased contact between the milling media and the slag, high kinetic energy in the mill, and wet operation..
- the reactivity of the slag can be controlled through the control of milling parameters and not dependent on any extraneous chemical addition. 4.
- the products developed by the process of present invention are superior in terms of reactivity, early start of hydration and complete and faster hydration properties then the products produced by any of the existing processes.
- the products developed by the process of present invention are superior in terms of crystallinity after hydration reactions then the products produced by the existing processes.
Abstract
Description
Claims
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA 2645348 CA2645348A1 (en) | 2006-03-10 | 2006-07-31 | A process for the production of reactive blast furnace slag |
EP20060779912 EP1993968A1 (en) | 2006-03-10 | 2006-07-31 | A process for the production of reactive blast furnace slag |
AU2006340282A AU2006340282A1 (en) | 2006-03-10 | 2006-07-31 | A process for the production of reactive blast furnace slag |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
IN641/DEL/2006 | 2006-03-10 | ||
IN641DE2006 | 2006-03-10 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007105029A1 true WO2007105029A1 (en) | 2007-09-20 |
Family
ID=37306055
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/IB2006/002077 WO2007105029A1 (en) | 2006-03-10 | 2006-07-31 | A process for the production of reactive blast furnace slag |
Country Status (6)
Country | Link |
---|---|
EP (1) | EP1993968A1 (en) |
KR (1) | KR20080102294A (en) |
CN (1) | CN101405237A (en) |
AU (1) | AU2006340282A1 (en) |
CA (1) | CA2645348A1 (en) |
WO (1) | WO2007105029A1 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2215031A1 (en) * | 2007-11-12 | 2010-08-11 | Procedo Enterprises Etablissement | Method for processing of pozzolans. |
WO2017194329A1 (en) | 2016-05-09 | 2017-11-16 | Construction Research & Technology Gmbh | Method for treatment of slag |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109437611B (en) * | 2018-11-08 | 2021-10-08 | 广东同创科鑫环保有限公司 | Sulfate-excitation-based solid waste cementing material |
CN109970378B (en) * | 2019-04-16 | 2022-03-25 | 山东大学 | Preparation process of solid waste base gelling material based on synergistic theory and carbonization/high temperature technology |
CN112608042A (en) * | 2020-12-19 | 2021-04-06 | 湖北工业大学 | Method for preparing superfine copper tailing filling cementing material by wet grinding method of water-quenched copper slag |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB246792A (en) * | 1925-01-30 | 1926-07-29 | Allis Chalmers Mfg Co | Improvements relating to process of treating slurry |
US3565648A (en) * | 1966-10-13 | 1971-02-23 | Kajima Construction Co Ltd | Method of utilizing blast furnace slag as a strength-improving agent for hardened cement |
US5804175A (en) * | 1993-04-30 | 1998-09-08 | Ronin; Vladimir P. | Method for producing cement |
GB2351973A (en) * | 1999-07-13 | 2001-01-17 | Petroleo Brasileiro Sa | Storable compositions and slurries for cementing oil and gas wells |
-
2006
- 2006-07-31 KR KR20087024594A patent/KR20080102294A/en not_active Application Discontinuation
- 2006-07-31 WO PCT/IB2006/002077 patent/WO2007105029A1/en active Application Filing
- 2006-07-31 CA CA 2645348 patent/CA2645348A1/en not_active Abandoned
- 2006-07-31 CN CNA2006800539792A patent/CN101405237A/en active Pending
- 2006-07-31 AU AU2006340282A patent/AU2006340282A1/en not_active Abandoned
- 2006-07-31 EP EP20060779912 patent/EP1993968A1/en not_active Withdrawn
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB246792A (en) * | 1925-01-30 | 1926-07-29 | Allis Chalmers Mfg Co | Improvements relating to process of treating slurry |
US3565648A (en) * | 1966-10-13 | 1971-02-23 | Kajima Construction Co Ltd | Method of utilizing blast furnace slag as a strength-improving agent for hardened cement |
US5804175A (en) * | 1993-04-30 | 1998-09-08 | Ronin; Vladimir P. | Method for producing cement |
GB2351973A (en) * | 1999-07-13 | 2001-01-17 | Petroleo Brasileiro Sa | Storable compositions and slurries for cementing oil and gas wells |
Non-Patent Citations (4)
Title |
---|
DATABASE COMPENDEX [online] ENGINEERING INFORMATION, INC., NEW YORK, NY, US; KUMAR RAKESH ET AL: "Hydration of mechanically activated granulated blast furnace slag", XP002408004, Database accession no. E2006059668041 * |
DATABASE COMPENDEX [online] ENGINEERING INFORMATION, INC., NEW YORK, NY, US; KUMAR S ET AL: "Improved processing of blended slag cement through mechanical activation", XP002408005, Database accession no. E2004348316285 * |
KUMAR R. ET AL: "Hydration of mechanically activated granulated blast furnace slag", METALLURGICAL AND MATERIALS TRANSACTIONS B: PROCESS METALLURGY AND MATERIALS PROCESSING SCIENCE DECEMBER 2005, vol. 36, no. 6, December 2005 (2005-12-01), US, pages 873 - 883, XP009075114 * |
KUMAR S ET AL: "Improved processing of blended slag cement through mechanical activation", JOURNAL OF MATERIALS SCIENCE, vol. 39, no. 10, 15 May 2004 (2004-05-15), US, pages 3449 - 3452, XP002408001 * |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP2215031A1 (en) * | 2007-11-12 | 2010-08-11 | Procedo Enterprises Etablissement | Method for processing of pozzolans. |
EP2215031A4 (en) * | 2007-11-12 | 2011-11-16 | Procedo Entpr Etablissement | Method for processing of pozzolans. |
WO2017194329A1 (en) | 2016-05-09 | 2017-11-16 | Construction Research & Technology Gmbh | Method for treatment of slag |
JP2019515868A (en) * | 2016-05-09 | 2019-06-13 | コンストラクション リサーチ アンド テクノロジー ゲーエムベーハーConstruction Research & Technology GmbH | How to process slag |
RU2739978C2 (en) * | 2016-05-09 | 2020-12-30 | Констракш Рисерч Энд Текнолоджи Гмбх | Slag treatment method |
AU2017262533B2 (en) * | 2016-05-09 | 2021-05-06 | Construction Research & Technology Gmbh | Method for treatment of slag |
JP7021111B2 (en) | 2016-05-09 | 2022-02-16 | コンストラクション リサーチ アンド テクノロジー ゲーエムベーハー | How to handle slag |
Also Published As
Publication number | Publication date |
---|---|
CN101405237A (en) | 2009-04-08 |
CA2645348A1 (en) | 2007-09-20 |
EP1993968A1 (en) | 2008-11-26 |
KR20080102294A (en) | 2008-11-24 |
AU2006340282A1 (en) | 2007-09-20 |
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