KR930021567A - 벽돌 원료로서의 전기 아크로 분진 - Google Patents
벽돌 원료로서의 전기 아크로 분진 Download PDFInfo
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- KR930021567A KR930021567A KR1019930005990A KR930005990A KR930021567A KR 930021567 A KR930021567 A KR 930021567A KR 1019930005990 A KR1019930005990 A KR 1019930005990A KR 930005990 A KR930005990 A KR 930005990A KR 930021567 A KR930021567 A KR 930021567A
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Abstract
벽돌 제조 공정에는 전기 아크로 분진을 소성한 다음 이 분진을 벽돌 원료와 혼합하고 이어서 이 혼합물을 벽돌로 성형하고 굽는 단계가 포함된다. EAF 분진을 미리 소성시키면 미리 소성시키지 않은 분진 자체를 통합시킨 벽돌과 비교할때 분진의 체적 밀도가 상당히 증가하고 훨씬 높은 압축강도를 갖는 벽돌을 제공하게 된다. 소성 공정시 생성된 휘발성의 재응축 중금속을 수집하고 정제한다. 소성 공정시 휘발성 중금속을 분리 및 수집한 결과 벽돌을 굽는 과정에서 실질적으로 중금속이 휘발되지 않는다.
Description
본 내용은 요부공개 건이므로 전문내용을 수록하지 않았음
제1도는 벽돌 제조를 위한 본 발명의 구체예에 따른 공정을 나타내는 플로우 다이아그램.
제2도는 소정시 EAF분진 시료의 온도에 따른 중량% 변화를 나타내는 그래프.
Claims (25)
- 전기 아크로 분진을 약 1040℃이상의 온도까지 가열하여 분진의 체적 밀도를 실질적으로 증가시키고 소정전기 아크로 분진을 형성시키는 전기 아크로 분진의 소정 단계와 상기 소성분진을 벽돌원료와 혼합하여 상기 소성분진이 약 60중량%까지 존재하는 혼합물을 형성하는 혼합단계 및 이 혼합물을 벽돌로 성형하고 이 성형 벽돌을 약 900-1370℃의 온도에서 굽는 단계로 이루어진 제철공정에서 작은 조각을 용해시키기 위해 적용되는 전기 아크로에서 생성된 전기 아크로 분진이 함유된 벽돌을 제조하는 방법.
- 제1항에 있어서, 상기 혼합물에는 소성 분진이 약 20-60중량% 함유됨을 특징으로 하는 방법.
- 제1항에 있어서, 상기 전기 아크로 분진은 1260℃ 까지의 온도에서 소성됨을 특징으로 하는 방법.
- 제1항에 있어서, 상기 전기 아크로 분진은 약 1120℃ 이상의 온도에서 소성됨을 특징으로 하는 방법.
- 제1항에 있어서, 상기 전기 아크로 분진은 약 1175-1205℃의 온도에서 소성됨을 특징으로 하는 방법.
- 제1항에 있어서, 상기 분진을 소성시키기 전에 적어도 하나의 환원제를 상기 전기아크로 분진의 전체 중량을 기준으로 하여 약 20중량%까지 상기 전기 아크로 분진에 첨가하는 부가적인 단계를 포함시키는 것을 특징으로 하는 방법.
- 제6항에 있어서, 환원제는 석탄과 코크, 톱밥, 폐유 및 작은 조각의 전선 절연체로 이루어진 군중에서 선택되는 적어도 하나임을 특징으로 하는 방법.
- 제6항에 있어서, 환원제는 상기 분진을 소성하기 전에 석탄을 전기 아크로 분진을 기준으로 하여 약 1중량%로 첨가됨을 특징으로 하는 방법.
- 제1항에 있어서, 상기 분진을 소성하기 전에 적어도 하나의 할로겐을 상기 전기 아크로 분진의 전체 중량을 기준으로 하여 약 6중량%까지 상기 전기 아크로 분진에 첨가시키는 부가적인 단계가 포함됨을 특징으로 하는 방법.
- 제9항에 있어서, 할로겐은 염소임을 특징으로 하는 방법.
- 제9항에 있어서, 할로겐은 전기 아크로 분진의 양을 기준으로 하여 약 2중량%의 염소인 것을 특징으로 하는 방법.
- 제1항에 있어서, 소성된 전기 아크로 분진의 체적 밀도는 적어도 129.3 1b/ft3임을 특징으로 하는 방법.
- 제1항에 있어서, 소성된 전기 아크로 분진의 체적 밀도는 적어도 139.5 1b/ft3임을 특징으로 하는 방법.
- 제1항에 있어서, 상기 소성 전기 아크로 분진의 체적 밀도는 소성전의 분진의 체적 밀도보다 적어도 4배 더 큼을 특징으로 하는 방법.
- 제1항에 있어서, 벽돌은 약 980-1100℃의 온도에서 소성시키는 것을 특징으로 하는 방법.
- 제1항에 있어서, 분진은 적어도 0.5시간 소성시키는 것을 특징으로 하는 방법.
- 제1항에 있어서, 블럭은 적어도 8시간 동안 소성시키는 것을 특징으로 하는 방법.
- 제1항에 있어서, 실질적으로 어떠한 가스 제거 단계가 없는 부가적인 가열 요건을 위해 가열된 가스를 재순환시키는 단계가 더욱 포함되어 가열단계시 분진을 가열하는 기체가 분진과 접촉되지 않는 것을 특징으로 하는 방법.
- 전기 아크로 분진을 약 1040℃ 이상의 온도에서 미리 소성시키고 체적 밀도가 적어도 약 129.3 1b/ft3인 것을 특징으로 하는 벽돌 원료 40-80중량%와 전기 아크로 분진 20-60중량%로 이루어진 벽돌.
- 제19항에 있어서, 상기 전기 아크로 분진은 소성전의 분진의 체적 밀도보다 적어도 4배 이상인 체적 밀도를 가짐을 특징으로 하는 벽돌.
- 제19항에 있어서, 적어도 하나의 할로겐이 미량으로 더욱 포함됨을 특징으로 하는 벽돌.
- 제19항에 있어서, 적어도 1500psi의 압축강도를 가짐을 특징으로 하는 벽돌.
- 제19항에 있어서, 약 0.2mg/L 이하의 용해율을 가짐을 특징으로 하는 벽돌.
- 제23항에 있어서, 적어도 1500psi의 압축강도를 가짐을 특징으로 하는 벽돌.
- ※ 참고사항 : 최초출원 내용에 의하여 공개하는 것임.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US7/866,364 | 1992-04-10 | ||
US07/866,364 | 1992-04-10 | ||
US07/866,364 US5278111A (en) | 1992-04-10 | 1992-04-10 | Electric arc furnace dust as raw material for brick |
Publications (2)
Publication Number | Publication Date |
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KR930021567A true KR930021567A (ko) | 1993-11-22 |
KR100223719B1 KR100223719B1 (ko) | 1999-10-15 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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KR1019930005990A KR100223719B1 (ko) | 1992-04-10 | 1993-04-09 | 벽돌 원료로서의 전기 아크로 분진 |
Country Status (8)
Country | Link |
---|---|
US (1) | US5278111A (ko) |
JP (1) | JP3405758B2 (ko) |
KR (1) | KR100223719B1 (ko) |
BR (1) | BR9301502A (ko) |
CA (1) | CA2093615C (ko) |
DE (1) | DE4311545B4 (ko) |
FR (1) | FR2689881B1 (ko) |
GB (1) | GB2265897B (ko) |
Families Citing this family (16)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2137090A1 (en) * | 1994-12-01 | 1996-06-02 | Jay Aota | Eaf dust treatment |
FR2737503B1 (fr) * | 1995-08-04 | 1997-10-10 | Wheelabrator Allevard | Procede de preparation de pigments mineraux, pigments mineraux ainsi obtenus, et installation pour la mise en oeuvre d'un tel procede |
DE19629099A1 (de) * | 1996-06-25 | 1998-01-02 | Anton Grehl | Verfahren zur Herstellung eines keramischen Formkörpers |
KR970026982A (ko) * | 1996-07-26 | 1997-06-24 | 김회수 | 적벽돌 및 그 제조방법 |
US5779949A (en) * | 1996-08-14 | 1998-07-14 | Indiana University Foundation | Conversion of lead-contaminated soil into ceramic products |
JP3504818B2 (ja) | 1997-02-28 | 2004-03-08 | 矢崎総業株式会社 | データ通信方法、及びこの方法を用いたデータ通信システム |
JP3220049B2 (ja) | 1997-05-27 | 2001-10-22 | 矢崎総業株式会社 | 通信方法、及び通信システム |
US5853474A (en) * | 1997-06-02 | 1998-12-29 | Conversion Systems, Inc. | Use of stabilized EAFD as a raw material in the production of a portland cement clinker |
KR19990007639A (ko) * | 1998-10-15 | 1999-01-25 | 이기강 | 고상폐기물을 원료로 하는 세라믹 조성물 및 이의 제조방법 |
US6682586B2 (en) | 2001-10-09 | 2004-01-27 | Heritage Environmental Services, Llc. | Assemblies and methods for processing zinc-bearing materials |
US20030110992A1 (en) | 2001-12-13 | 2003-06-19 | Pavlik Robert S. | Alumina refractories and methods of treatment |
JP2005239473A (ja) * | 2004-02-25 | 2005-09-08 | Koyo Seiko Co Ltd | 窯業製品用の呈色剤及びこれを用いた発色粘土 |
US7648933B2 (en) * | 2006-01-13 | 2010-01-19 | Dynamic Abrasives Llc | Composition comprising spinel crystals, glass, and calcium iron silicate |
US9278888B1 (en) | 2012-11-01 | 2016-03-08 | Saudi Basic Industries Corporation | Use of non-chloride cement accelerator and electric arc furnace dust in cement |
RU2655323C1 (ru) * | 2017-05-29 | 2018-05-25 | федеральное государственное автономное образовательное учреждение высшего образования "Самарский национальный исследовательский университет имени академика С.П. Королёва" | Керамическая композиция для изготовления легковесного кирпича |
CN113621797A (zh) * | 2021-08-18 | 2021-11-09 | 江西金洋金属股份有限公司 | 一种脱硫铅膏砖及其制备方法 |
Family Cites Families (14)
Publication number | Priority date | Publication date | Assignee | Title |
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DE2400037A1 (de) * | 1974-01-02 | 1975-07-10 | Andreas Haessler | Verfahren zur herstellung von leichtziegeln |
DE2611213C3 (de) * | 1976-03-17 | 1979-11-08 | Steag Ag, 4300 Essen | Verfahren und Anlage zur Herstellung von Ziegeln, insbesondere von Klinkern aus einer Mischung, in die ein aus insbesondere Steinkohlenkraftwerken stammender Flugstaub eingesetzt wird |
US4047884A (en) * | 1976-04-05 | 1977-09-13 | Allis-Chalmers Corporation | Means and method for processing cement raw materials containing fuel of high volatile content |
US4130439A (en) * | 1977-02-24 | 1978-12-19 | Gashenko Stanislav I | Method of preparing batch for manufacture of clay brick |
JPS53127511A (en) * | 1977-04-14 | 1978-11-07 | Daido Steel Co Ltd | Process for making colored ceramics |
SU753828A1 (ru) * | 1978-07-24 | 1980-08-07 | Государственный Всесоюзный Научно- Исследовательский Институт Строительных Материалов И Конструкций Им. П.П. Будникова | Керамическа масса |
JPS582264A (ja) * | 1981-06-27 | 1983-01-07 | 東京鉄鋼株式会社 | 製鋼ダストの処理方法 |
DE3414399A1 (de) * | 1984-04-17 | 1985-10-24 | Georg Dr.phil.nat. Dipl.-Chem. 4620 Castrop-Rauxel Fritsch | Verfahren zur entsorgung metallurgischer industrien von eisenhaltigen, staub- oder schlammfoermigen abgaengen, z.b. von filterstaeuben |
NL8403501A (nl) * | 1984-11-15 | 1986-06-02 | Pelt & Hooykaas | Werkwijze voor het omzetten in onschadelijke vorm van bij chemische of fysische werkwijzen vrijkomende deeltjes door mengen met een gesmolten silicaathoudend materiaal alsmede gevormd materiaal. |
DD244547A1 (de) * | 1985-12-20 | 1987-04-08 | Florin Stahl Walzwerk | Keramisches material |
DE3713482A1 (de) * | 1987-04-22 | 1988-11-10 | Kurt Kretschmann | Verfahren zur umweltschonenden entsorgung von schwermetallhaltigen rueckstaenden aus muellverbrennungsanlagen oder dergleichen |
DE3716484A1 (de) * | 1987-05-16 | 1988-11-24 | Georg Dipl Chem Dr Phi Fritsch | Verfahren zur herstellung eines lagerfaehigen, insbesondere eines deponiefaehigen erzeugnisses aus einem eisenhaltigen, feinkoernigen abgang enthaltend freies sechswertiges chrom, beispielsweise filterstaub der elektrostahlherstellung |
ZA883753B (en) * | 1987-06-18 | 1989-03-29 | Bethlehem Steel Corp | Process for chemical stabilization of heavy metal bearing dusts and sludge,such as eaf dust |
IT1236816B (it) * | 1989-11-22 | 1993-04-02 | Contento Trade Sas Di C M P | Procedimento per il recupero di rifiuti industriali. |
-
1992
- 1992-04-10 US US07/866,364 patent/US5278111A/en not_active Expired - Lifetime
-
1993
- 1993-04-05 FR FR9303997A patent/FR2689881B1/fr not_active Expired - Fee Related
- 1993-04-06 GB GB9307115A patent/GB2265897B/en not_active Expired - Fee Related
- 1993-04-07 DE DE4311545A patent/DE4311545B4/de not_active Expired - Fee Related
- 1993-04-07 CA CA002093615A patent/CA2093615C/en not_active Expired - Fee Related
- 1993-04-09 JP JP10762193A patent/JP3405758B2/ja not_active Expired - Fee Related
- 1993-04-09 KR KR1019930005990A patent/KR100223719B1/ko not_active IP Right Cessation
- 1993-04-12 BR BR9301502A patent/BR9301502A/pt not_active Application Discontinuation
Also Published As
Publication number | Publication date |
---|---|
DE4311545B4 (de) | 2004-12-09 |
CA2093615C (en) | 2004-07-06 |
KR100223719B1 (ko) | 1999-10-15 |
GB9307115D0 (en) | 1993-05-26 |
GB2265897B (en) | 1996-01-10 |
FR2689881B1 (fr) | 1996-06-07 |
BR9301502A (pt) | 1993-10-13 |
US5278111A (en) | 1994-01-11 |
DE4311545A1 (de) | 1993-10-14 |
FR2689881A1 (fr) | 1993-10-15 |
JPH0648817A (ja) | 1994-02-22 |
GB2265897A (en) | 1993-10-13 |
JP3405758B2 (ja) | 2003-05-12 |
CA2093615A1 (en) | 1993-10-11 |
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