EP1664353B2 - Procede et installation pour granuler des scories - Google Patents
Procede et installation pour granuler des scories Download PDFInfo
- Publication number
- EP1664353B2 EP1664353B2 EP04765337A EP04765337A EP1664353B2 EP 1664353 B2 EP1664353 B2 EP 1664353B2 EP 04765337 A EP04765337 A EP 04765337A EP 04765337 A EP04765337 A EP 04765337A EP 1664353 B2 EP1664353 B2 EP 1664353B2
- Authority
- EP
- European Patent Office
- Prior art keywords
- water
- slag
- granulation
- gases
- condensation
- 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.)
- Expired - Lifetime
Links
- 239000002893 slag Substances 0.000 title claims abstract description 49
- 238000000034 method Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 85
- 239000007789 gas Substances 0.000 claims abstract description 56
- 238000005469 granulation Methods 0.000 claims abstract description 34
- 230000003179 granulation Effects 0.000 claims abstract description 34
- 238000002347 injection Methods 0.000 claims abstract description 26
- 239000007924 injection Substances 0.000 claims abstract description 26
- 239000008187 granular material Substances 0.000 claims abstract description 18
- 238000009833 condensation Methods 0.000 claims abstract description 17
- 230000005494 condensation Effects 0.000 claims abstract description 17
- 238000009434 installation Methods 0.000 claims abstract description 16
- 239000000203 mixture Substances 0.000 claims abstract description 9
- 238000003723 Smelting Methods 0.000 claims abstract description 6
- 238000002485 combustion reaction Methods 0.000 claims description 15
- 230000004888 barrier function Effects 0.000 claims description 5
- 239000007921 spray Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 3
- 239000003546 flue gas Substances 0.000 claims 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 5
- 239000011593 sulfur Substances 0.000 description 5
- 229910052717 sulfur Inorganic materials 0.000 description 5
- 238000001816 cooling Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 238000010079 rubber tapping Methods 0.000 description 3
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 description 2
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 239000000292 calcium oxide Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000008092 positive effect Effects 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B3/00—General features in the manufacture of pig-iron
- C21B3/04—Recovery of by-products, e.g. slag
- C21B3/06—Treatment of liquid slag
- C21B3/08—Cooling slag
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2100/00—Handling of exhaust gases produced during the manufacture of iron or steel
- C21B2100/40—Gas purification of exhaust gases to be recirculated or used in other metallurgical processes
- C21B2100/42—Sulphur removal
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/022—Methods of cooling or quenching molten slag
- C21B2400/024—Methods of cooling or quenching molten slag with the direct use of steam or liquid coolants, e.g. water
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/03—Removing sulfur
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/02—Physical or chemical treatment of slags
- C21B2400/032—Separating slag from liquid, e.g. from water, after quenching
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/062—Jet nozzles or pressurised fluids for cooling, fragmenting or atomising slag
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/066—Receptacle features where the slag is treated
- C21B2400/072—Tanks to collect the slag, e.g. water tank
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21B—MANUFACTURE OF IRON OR STEEL
- C21B2400/00—Treatment of slags originating from iron or steel processes
- C21B2400/05—Apparatus features
- C21B2400/066—Receptacle features where the slag is treated
- C21B2400/074—Tower structures for cooling, being confined but not sealed
Definitions
- the invention relates to a method for granulating slag, in particular from a blast furnace and / or a smelting reduction plant, wherein a granulate-water mixture formed during granulation is fed to a granulation vessel and then to a dewatering plant in which the slag granules are dehydrated, and wherein the Granulating resulting H 2 S-containing vapors and gases are at least partially condensed in a congruent with the Grenulier disposer condensing space by injecting water.
- the air introduced into the system leads in other plant areas according to DE 35 11 958 C to a slight overpressure and passes through Granulatabsch- and other openings as well as over covers in the atmosphere. With the air, however, the harmful gases in concentrations that are above the permitted limits escape uncontrolled into the atmosphere.
- an overpressure is set in the granulating container and in the condenser space below the water injection. This is done by setting the water injection.
- the overpressure has the positive effect that the H 2 S-containing residual gases without forced delivery devices, such as fans and the like., Are passed to the downstream combustion point, ie slag trough.
- the amount of air introduced into the granulator reduces the amount of air and H 2 S cargo discharged from the system.
- the sulfur-containing vapors and gases produced during granulation are precipitated in a condensing tower 10 arranged above the granulation container 4.
- a device 11 for water injection is arranged, which is supplied via a fed from the collecting tank 23 water supply 12 with calcium oxide-containing water.
- a means 13 for collecting water and condensate e.g. formed by water gutters, arranged, which upper a discharge line 14 is connected to the water basin 7c.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Furnace Details (AREA)
- Manufacture Of Iron (AREA)
- Processing Of Solid Wastes (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Claims (15)
- Procédé pour granuler des scories, en particulier d'un haut fourneau et/ou d'une installation de réduction en fusion, dans lequel un mélange eau-granulat formé lors de la granulation est envoyé à un récipient de granulation (4) et ensuite à une installation d'assèchement, dans laquelle les scories granulées sont asséchées, et dans lequel les vapeurs et les gaz contenant du H2S produits pendant la granulation sont condensés au moins en partie par injection d'eau dans une chambre de condensation communiquant par écoulement avec le récipient de granulation (4), les gaz résiduels contenant du H2S étant déviés hors de la chambre de condensation par une conduite d'évacuation (15) en dessous de l'injection d'eau et le H2S étant brûlé, caractérisé en ce que les gaz résiduels sont introduits dans le canal à scories (1) entre le dispositif de granulation (2) et une hotte aspirante (18) prévue au-dessus du canal à scories (1) et guidés à contre-courant par rapport aux scories chaudes, où, grâce à la distance entre la sortie de la conduite d'évacuation (15) dans le canal à scories (1) et la hotte aspirante (18), les gaz résiduels se réchauffent à la température nécessaire pour la combustion de H2S, le cas échéant avec apport de chaleur au moyen d'une flamme d'appoint, et on dispose de suffisamment de temps pour la combustion afin que le H2S soit pendant ce temps brûlé en SO2, les gaz résiduels de combustion étant déviés via la hotte aspirante (18) et le cas échéant alimentés dans un refroidisseur à l'eau ou un dispositif de dépoussiérage.
- Procédé selon la revendication 1, caractérisé en ce que les gaz d'échappement de la combustion sont refroidis à l'eau et le SO2 provenant du H2S est précipité.
- Procédé selon l'une quelconque des revendications 1 ou 2, caractérisé en ce que le récipient de granulation (4) est séparé de façon étanche au gaz par rapport à l'installation d'assèchement.
- Procédé selon l'une quelconque des revendications 1 à 3, caractérisé en ce que l'on établit une surpression dans le récipient de granulation (4) et dans la chambre de condensation en dessous de l'injection d'eau.
- Procédé selon l'une quelconque des revendications 1 à 4, caractérisé en ce que les vapeurs et les gaz produits dans l'installation d'assèchement sont conduits dans la chambre de condensation au-dessus de l'injection d'eau.
- Procédé selon la revendication 5, caractérisé en ce que l'on établit une dépression dans la chambre de condensation au-dessus de l'injection d'eau.
- Procédé selon la revendication 5 ou 6, caractérisé en ce que la quantité de vapeurs et de gaz conduite dans la chambre de condensation au moyen d'un effet d'aspiration est régulée par la quantité d'eau injectée et est maintenue à un niveau minimum.
- Procédé selon l'une quelconque des revendications 1 à 7, caractérisé en ce que le condensat formé dans la chambre de condensation et l'eau injectée sont évacués hors de la chambre de condensation et ajoutés à l'eau précipitée dans l'installation d'assèchement, qui est recyclée pour la granulation et pour l'injection d'eau.
- Procédé selon l'une quelconque des revendications 1 à 8, caractérisé en ce que la quantité d'eau injectée est régulée en fonction du débit de scories.
- Installation pour granuler des scories, en particulier d'un haut fourneau et/ou d'une installation de réduction en fusion, comprenant un canal à scories (1) pourvu d'une hotte aspirante (18) pour transporter les scories chaudes vers un dispositif (2) de granulation, de préférence une tête de projection, un récipient de granulation (4) disposé ensuite pour recueillir un mélange eau-granulat, un dispositif de condensation (10) communiquant en écoulement avec le récipient de granulation (4), de préférence une tour de condensation, avec une arrivée d'eau (12) et un dispositif (11) pour l'injection d'eau, et une installation d'assèchement du granulat, caractérisée en ce qu'il est prévu dans le dispositif de condensation (10), en dessous du dispositif (11) pour l'injection d'eau, une conduite d'évacuation (15) pour les vapeurs et les gaz, qui débouche dans le canal à scories (1) entre le dispositif de granulation (2) et la hotte aspirante (18), en ce que les vapeurs et les gaz peuvent être guidés à contre-courant par rapport aux scories chaudes, où, grâce à la distance entre la sortie de la conduite d'évacuation (15) dans le canal à scories (1) et la hotte aspirante (18), les vapeurs et les gaz se réchauffent à la température nécessaire pour la combustion de H2S et on dispose de suffisamment de temps pour la combustion afin que le H2S soit pendant ce temps brûlé en SO2, un refroidisseur à l'eau (17) ou un dispositif de dépoussiérage étant prévu pour l'évacuation des gaz de combustion hors de la hotte aspirante (18) dans le refroidisseur à l'eau (17) ou dans le dispositif de dépoussiérage.
- Installation selon la revendication 10, caractérisé en ce que le canal à scories (1) comporte un brûleur (19) pour la production d'une flamme d'appoint.
- Installation selon l'une quelconque des revendications 10 ou 11, caractérisé en ce que l'installation d'assèchement de granulat comprend au moins un dispositif d'assèchement (6a, 6b) et un bassin à eau (7a, 7b, 7c), qui sont pourvus d'une hotte de recouvrement (21a, 21b, 21c), et de la hotte de recouvrement (21a, 21b, 21c) part une conduite d'évacuation (22) pour des vapeurs et des gaz, qui débouche dans le dispositif de condensation (10) au-dessus du dispositif (11) pour l'injection d'eau.
- Installation selon l'une quelconque des revendications 10 à 12, caractérisée en ce qu'il est prévu un barrage à gaz (20) entre le récipient de granulation (4) et l'installation d'assèchement du granulat.
- Installation selon l'une quelconque des revendications 10 à 13, caractérisée en ce qu'il est prévu dans le dispositif de condensation (10), en dessous du dispositif (11) pour l'injection d'eau, un moyen (13) pour capter l'eau et le condensat, duquel part une conduite d'évacuation (14) qui débouche dans le dispositif d'assèchement du granulat, en particulier dans le bassin à eau (7c).
- Installation selon l'une quelconque des revendications 10 à 14, caractérisée en ce que l'installation d'assèchement du granulat, en particulier le bassin à eau (7c), est en liaison de communication avec l'arrivée d'eau (12) du dispositif de condensation (10) et/ou du dispositif de granulation (2).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL04765337T PL1664353T5 (pl) | 2003-09-25 | 2004-09-17 | Sposób i instalacja do granulacji żużla |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT0152503A AT412650B (de) | 2003-09-25 | 2003-09-25 | Verfahren und anlage zum granulieren von schlacke |
PCT/EP2004/010442 WO2005031008A1 (fr) | 2003-09-25 | 2004-09-17 | Procede et installation pour granuler des scories |
Publications (3)
Publication Number | Publication Date |
---|---|
EP1664353A1 EP1664353A1 (fr) | 2006-06-07 |
EP1664353B1 EP1664353B1 (fr) | 2007-01-17 |
EP1664353B2 true EP1664353B2 (fr) | 2011-10-12 |
Family
ID=33136548
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP04765337A Expired - Lifetime EP1664353B2 (fr) | 2003-09-25 | 2004-09-17 | Procede et installation pour granuler des scories |
Country Status (14)
Country | Link |
---|---|
US (2) | US7600397B2 (fr) |
EP (1) | EP1664353B2 (fr) |
KR (1) | KR101186277B1 (fr) |
CN (1) | CN1856583B (fr) |
AT (2) | AT412650B (fr) |
AU (1) | AU2004276445B2 (fr) |
BR (1) | BRPI0414805A (fr) |
CA (1) | CA2539601A1 (fr) |
DE (1) | DE502004002708D1 (fr) |
ES (1) | ES2280998T5 (fr) |
PL (1) | PL1664353T5 (fr) |
PT (1) | PT1664353E (fr) |
RU (1) | RU2355771C2 (fr) |
WO (1) | WO2005031008A1 (fr) |
Families Citing this family (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP5055285B2 (ja) | 2005-09-30 | 2012-10-24 | タータ スチール リミテッド | 鋼プラント廃棄物及び廃熱から水素及び(又は)他の気体を製造する方法 |
EP2013139A4 (fr) * | 2006-04-28 | 2009-12-16 | Tata Steel Ltd | Installation pour la production de gaz hydrogène par décomposition thermochimique de l'eau en utilisant des laitiers et des rejets d'aciérie |
KR100709061B1 (ko) * | 2006-09-29 | 2007-04-18 | 주식회사 티아이엔지니어링건축사사무소 | 건축용 안전창호 구조 |
JP5303977B2 (ja) * | 2008-03-20 | 2013-10-02 | Jfeスチール株式会社 | スラグの処理方法 |
LU91626B1 (en) * | 2009-12-03 | 2011-06-06 | Wurth Paul Sa | Installation and method for processing molten material produced by a metallurgical plant, in particular for processing blast furnace slag |
LU91765B1 (en) * | 2010-12-14 | 2012-06-15 | Wurth Paul Sa | Steam condensation tower for a granulation installation |
CN103060494B (zh) * | 2013-01-09 | 2016-01-27 | 北京世纪源博科技股份有限公司 | 一种蒸汽回收型高炉冲渣水系统 |
CN103060498B (zh) * | 2013-01-09 | 2015-03-11 | 北京世纪源博科技股份有限公司 | 一种高炉冲渣水余热发电系统 |
CN103555870B (zh) * | 2013-10-30 | 2015-07-01 | 江苏沙钢集团有限公司 | 一种无冷却塔型高温炉渣水淬冷凝工艺及系统 |
RU2017110486A (ru) * | 2014-09-21 | 2018-10-01 | Хэтч Лтд. | Газовое распыление расплавленных материалов с использованием побочных отходящих газов |
CN108707709B (zh) * | 2018-08-21 | 2023-07-25 | 北京京诚科林环保科技有限公司 | 一种高炉水渣粒化塔正压粒化装置及正压粒化方法 |
CN109529560A (zh) * | 2018-12-27 | 2019-03-29 | 中冶京诚工程技术有限公司 | 一种高炉水渣系统过滤池蒸汽消白的方法 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4402492A (en) † | 1982-06-16 | 1983-09-06 | United States Steel Corporation | Burner apparatus for molten metal fume suppression |
US4475720A (en) † | 1983-03-14 | 1984-10-09 | Broom Gilbert R | Casthouse emission control system |
LU88441A1 (fr) † | 1993-12-16 | 1995-07-10 | Wurth Paul Sa | Procédé pour le traitement d'un mélange de vapeurs d'eau et d'air pollué par des gaz sulfurés |
Family Cites Families (16)
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US3738820A (en) * | 1970-06-01 | 1973-06-12 | Kinney S Eng Inc | Method of and apparatus for the processing of molten slag |
DE2253806C3 (de) * | 1972-11-03 | 1978-06-15 | Metallgesellschaft Ag, 6000 Frankfurt | Verfahren zur Umsetzung des in Gasgemischen enthaltenen Schwefelwasserstoffs mit Schwefeldioxid nach dem Claus-Prozess |
US3912487A (en) * | 1974-06-24 | 1975-10-14 | Mikhail Alexeevich Sharanov | Apparatus for producing granulated slag |
DE3511958A1 (de) * | 1985-04-02 | 1986-10-16 | AJO-Stahlbau GmbH & Co KG, 5905 Freudenberg | Verfahren und einrichtung zum herstellen von schlackensand (granulat) aus hochofenschlacke |
CN1009207B (zh) * | 1986-04-21 | 1990-08-15 | Ajo钢铁制造有限公司 | 由高炉炉渣制造炉渣砂(粒渣)的方法和装置 |
US5082483A (en) * | 1990-06-08 | 1992-01-21 | National Slag Limited | Enclosures for slag pelletization apparatus and method of operation thereof |
ATE134698T1 (de) * | 1991-11-29 | 1996-03-15 | Noell En Und Entsorgungstechni | Verfahren zur thermischen verwertung von abfallstoffen |
AU672698B2 (en) * | 1993-06-30 | 1996-10-10 | Mitsubishi Materials Corporation | Apparatus for water-granulating slag |
US5540895A (en) * | 1994-06-03 | 1996-07-30 | Paul Wurth S.A. | Device for the treatment of mixture of steam and air contaminated with sulphurous gases, formed during the granulation and dehydration of blast furnace slag |
LU88543A1 (fr) * | 1994-10-06 | 1996-04-29 | Wurth Paul Sa | Procédé pour la granulation humide de laitier |
JP2868432B2 (ja) * | 1995-03-08 | 1999-03-10 | ラサ商事株式会社 | 溶鉱炉溶滓の水砕システムにおける有害ガス処理方法および処理設備 |
GB9719512D0 (en) * | 1997-09-12 | 1997-11-19 | Boc Group Plc | Treatment of a combustible gas stream |
JP3947892B2 (ja) * | 1999-06-29 | 2007-07-25 | バブコック日立株式会社 | 硫黄分回収方法及びその硫黄分回収方法を適用したガス化プラント |
CN1140636C (zh) * | 2000-04-07 | 2004-03-03 | 张维田 | 炉渣粒化蒸汽冷凝回收装置 |
DE10152672C2 (de) * | 2001-10-05 | 2003-11-13 | Voest Alpine Ind Anlagen | Schlackengranulierungsanlage |
WO2003087669A1 (fr) * | 2002-04-12 | 2003-10-23 | Ebara Corporation | Incinerateur, incinerateur de gazeification et procede de traitement des dechets |
-
2003
- 2003-09-25 AT AT0152503A patent/AT412650B/de not_active IP Right Cessation
-
2004
- 2004-09-17 US US10/572,775 patent/US7600397B2/en not_active Expired - Fee Related
- 2004-09-17 CN CN2004800278280A patent/CN1856583B/zh not_active Expired - Fee Related
- 2004-09-17 BR BRPI0414805-3A patent/BRPI0414805A/pt active Search and Examination
- 2004-09-17 WO PCT/EP2004/010442 patent/WO2005031008A1/fr active IP Right Grant
- 2004-09-17 PL PL04765337T patent/PL1664353T5/pl unknown
- 2004-09-17 AT AT04765337T patent/ATE351927T1/de not_active IP Right Cessation
- 2004-09-17 CA CA002539601A patent/CA2539601A1/fr not_active Abandoned
- 2004-09-17 KR KR1020067007716A patent/KR101186277B1/ko not_active IP Right Cessation
- 2004-09-17 ES ES04765337T patent/ES2280998T5/es not_active Expired - Lifetime
- 2004-09-17 PT PT04765337T patent/PT1664353E/pt unknown
- 2004-09-17 RU RU2006113925/02A patent/RU2355771C2/ru not_active IP Right Cessation
- 2004-09-17 DE DE502004002708T patent/DE502004002708D1/de not_active Expired - Lifetime
- 2004-09-17 AU AU2004276445A patent/AU2004276445B2/en not_active Ceased
- 2004-09-17 EP EP04765337A patent/EP1664353B2/fr not_active Expired - Lifetime
-
2009
- 2009-08-28 US US12/549,832 patent/US8302430B2/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4402492A (en) † | 1982-06-16 | 1983-09-06 | United States Steel Corporation | Burner apparatus for molten metal fume suppression |
US4475720A (en) † | 1983-03-14 | 1984-10-09 | Broom Gilbert R | Casthouse emission control system |
LU88441A1 (fr) † | 1993-12-16 | 1995-07-10 | Wurth Paul Sa | Procédé pour le traitement d'un mélange de vapeurs d'eau et d'air pollué par des gaz sulfurés |
Non-Patent Citations (7)
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"Air pollution engineering manual", METALLUUGICAL INDUSTRY, 2000 - 2000, pages 565 - 573 † |
K-H. GROSSPIETSCH ET AL.: "Neue Schlackengranulationsanlage verbessert", STAHL UND EISEN, no. 8, 15 August 2003 (2003-08-15) - 15 August 2003 (2003-08-15), pages 61 - 67 † |
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Publication number | Publication date |
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PL1664353T5 (pl) | 2013-02-28 |
WO2005031008A1 (fr) | 2005-04-07 |
CN1856583B (zh) | 2010-12-01 |
RU2355771C2 (ru) | 2009-05-20 |
KR20060093337A (ko) | 2006-08-24 |
PT1664353E (pt) | 2007-04-30 |
ES2280998T5 (es) | 2012-02-17 |
US8302430B2 (en) | 2012-11-06 |
AT412650B (de) | 2005-05-25 |
PL1664353T3 (pl) | 2007-06-29 |
CA2539601A1 (fr) | 2005-04-07 |
US20090315233A1 (en) | 2009-12-24 |
KR101186277B1 (ko) | 2012-09-27 |
ATA15252003A (de) | 2004-10-15 |
CN1856583A (zh) | 2006-11-01 |
BRPI0414805A (pt) | 2006-11-14 |
EP1664353A1 (fr) | 2006-06-07 |
US20070107466A1 (en) | 2007-05-17 |
US7600397B2 (en) | 2009-10-13 |
EP1664353B1 (fr) | 2007-01-17 |
RU2006113925A (ru) | 2007-10-27 |
AU2004276445B2 (en) | 2009-11-12 |
AU2004276445A1 (en) | 2005-04-07 |
ES2280998T3 (es) | 2007-09-16 |
ATE351927T1 (de) | 2007-02-15 |
DE502004002708D1 (de) | 2007-03-08 |
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