[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

CN104874583A - Comprehensive treatment method of dry reclaimed dust of blast furnace - Google Patents

Comprehensive treatment method of dry reclaimed dust of blast furnace Download PDF

Info

Publication number
CN104874583A
CN104874583A CN201510227331.3A CN201510227331A CN104874583A CN 104874583 A CN104874583 A CN 104874583A CN 201510227331 A CN201510227331 A CN 201510227331A CN 104874583 A CN104874583 A CN 104874583A
Authority
CN
China
Prior art keywords
ash
blast furnace
dust
carbon
dry
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.)
Pending
Application number
CN201510227331.3A
Other languages
Chinese (zh)
Inventor
任天飞
杨琦云
张威
唐忠
潘伟
张德强
傅双波
王维
王建湘
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hunan Valin Xiangtan Iron and Steel Co Ltd
Hunan Hualing Xiangtan Iron and Steel Co Ltd
Original Assignee
Hunan Hualing Xiangtan Iron and Steel Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hunan Hualing Xiangtan Iron and Steel Co Ltd filed Critical Hunan Hualing Xiangtan Iron and Steel Co Ltd
Priority to CN201510227331.3A priority Critical patent/CN104874583A/en
Publication of CN104874583A publication Critical patent/CN104874583A/en
Pending legal-status Critical Current

Links

Landscapes

  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention relates to a comprehensive treatment method of dry reclaimed dust of a blast furnace. The reclaimed dust mainly comprise the following ingredients: 15-25% of TFe, 14-30% of C, 4-6% of Zn, 5-7% of alkali metal salt, 0.5-1.9% of cyanide, 8-10% of SiO2, 2-3% of Al2O3, 15-21% of CaO and MnO, and small amounts of combined-state Pb and Cu or simple substances Pb and Cu. The technological process comprises the steps of unloading the dust, mixing, carrying out ball milling, performing flotation, reselecting and carrying out water treatment. After the method is applied to the dry reclaimed dusts of the blast furnace, environment-protection indexes reach the standard, and the contents of alkali metal, lead and zinc entering ore matching for sintering directly can be reduced greatly; the yield of fine powdered iron in dry reclaimed dusts is improved by 5-10%, the yield of the recycled carbon dusts is improved by 8-10% and the equipment failure rate is reduced remarkably.

Description

The integrated conduct method of blast furnace dry type dedusting ash
Technical field
The invention belongs to comprehensive utilization of resources and environmental protection technical field, be specifically related to a kind of integrated conduct method of blast furnace dry type dedusting ash.
Background technology
Steel mill can carry out dry method dust to blast furnace dust, gas mud etc. usually, obtains a kind of dry dust removal ash (being called for short " dry method ash ").For certain steel enterprise, containing the alkalinous metal salinity of 5.0% ~ 7.0% in this blast furnace dry method dust ash, Zn content 4.0 % ~ 6.0%, cyanide content 0.05 % ~ 0.19 %, to alkali metal load and the Zn load of blast furnace be increased as directly returned Iron Ore Matching in Sintering, totally unfavorable to smooth operation of furnace.
Prior art generally adopts the method for cycling water ore dressing to this dedusting ash, and this this goes make recirculated water constantly concentrated and enrichment, salinity, CN in system -content rises, and pH value increases, and concerning surrounding environment being a larger hidden danger, and is greatly affected due to the higher ore-sorting system that makes of water quality basicity.Dissolve the salinity in ferrous material and cryanide ion in recirculated water, cause the salinity of system, cryanide ion higher.By the impact of technique, the harmful element content that dry method ash contains is higher, and through circulation, constantly concentrate, in recirculated water, salinity can reach about 12% ~ 13%, and cryanide ion can reach 1800 ~ 2000 ppm.
Along with the pay attention to day by day to environmental protection, it is enterprise's problem demanding prompt solution that the separation of dry method ash active ingredient and environmental protection utilize.
Summary of the invention
The object of the present invention is to provide a kind of integrated conduct method of blast furnace gas dry type bag-type dust ash.
Technical scheme of the present invention: the integrated conduct method of blast furnace dry type dedusting ash, described dedusting ash main component comprises: TFe=15% ~ 25%, C=14% ~ 30%, Zn=4% ~ 6%, alkali metal salt=5% ~ 7%, cyanide=0.5% ~ 1.9%, SiO 2=8% ~ 10%, Al 2o 3=2% ~ 3%, CaO+MgO=15% ~ 21%, all the other are a small amount of Pb, Cu chemical combination state or simple substance.Technological process comprises unloads ash-stirring-ball milling-flotation-gravity treatment-water treatment.Its processing step is:
(1) ash is unloaded: dry method ash unloads ash and puts into material pond and exist side by side and namely use recirculated water immersion treatment.
(2) stir: add water dry method ash the mud dispersed with stirring being configured to 20% ~ 30% concentration.
(3) ball milling: the ore pulp after stirring enters ball mill grinding, makes caking and coarse particulate matter obtain grinding dispersion.
(4) flotation: according to ore pulp after mineral grain fully disperses: floating agent: diesel oil=90 ~ 100: the ratio of 1 ~ 1.2: 0.35 ~ 0.45 stirs, utilize flotation device to be sorted out by carbon wherein, what obtain carbon containing > 75% utilizes carbon.
(5) gravity treatment: select the ore pulp after carbon to adopt spiral chute and shaking table to carry out gravity separation, the Iron concentrate obtained containing full iron 45% ~ 50% is recycled for sintering.
(6) water treatment: regularly add ferrous sulfate according to the amount of 50 ~ 70 times of cyanide ion concentration in water system, total cyanogen is reduced to 15 below ppm.
After Filter Press, filtrate is the waste water of alkali metal containing salt, also may be used for smelting iron washing slag water.After discharge of wastewater, production system replaces salary again.
Progressive effect of the present invention: after dry method ash implements the method, environmental protection index can be up to standard, greatly reduces the content of the alkali metal directly entering into Iron Ore Matching in Sintering, plumbous zinc simultaneously.In dry method ash, Iron concentrate recovery rate improves 5% ~ 10%, and reclaim carbon dust recovery rate and improve 8% ~ 10%, equipment failure rate obviously reduces.Because of a little, the inventive method, by reducing the harm of harmful element, can effectively utilize iron-containing waste, for the normal operation of blast furnace and the integrated treatment of blast furnace dry method ash provide a new method.
Detailed description of the invention
Embodiment 1: the integrated conduct method of blast furnace gas dry type bag-type dust ash
3# blast furnace dedusting ash Main Ingredients and Appearance content is as table 1.
Table 1 3# blast furnace dedusting ash Main Ingredients and Appearance content
Treatment process steps is:
(1) ash is unloaded: 3# blast furnace dry method ash 20t is put into material pond and exist side by side and namely use recirculated water immersion treatment.
(2) stir: use 5t clamshell crane to grab 5 buckets and put into the agitator that diameter is 2.5m, in agitator, add water 2.2 m deeply, being configured to pulp density is 26.2 %, stirs after 15 minutes for subsequent use in agitator.
(3) ball milling: the ore pulp after stirring enters ball mill and carries out ore grinding, makes bulk lump and coarse particulate matter obtains grinding dispersion, is convenient to the ore dressing resolution ratio of follow-up flotation and gravity separation technology.
(4) flotation: ore pulp enters 4A flotation device after ball mill, ore pulp is joined according to real: floating agent: diesel oil=98: the ratio of 1.01: 0.38 adds in agitator simultaneously carries out stirring reaction after mineral grain fully disperses, utilize 4A flotation device to carry out selecting carbon, the carbon content after flotation device flotation is 82.1%.Meet the requirement of iron-making coal-injecting to carbon content.
(5) gravity treatment: select the ore pulp after carbon to utilize the heavy physical property of iron compound to adopt spiral chute and shaking table to carry out gravity separation, the Iron concentrate obtained containing full iron 52.3% is recycled for sintering.
(6) water treatment: circulate after 35 days, cyanide ion concentration 1380 ppm in system, the water yield amounts to 300 tons, after adding ferrous sulfate, total cyanogen is reduced to 14.54 ppm.
After Filter Press, filtrate is the waste water of alkali metal containing salt, for smelting iron washing slag water.After discharge of wastewater, production system replaces salary again.
Before water treatment, system is after the circulation of 35 days, and potassium, sodium salt content=11.3 %, PH=13.4 in water, cyanide content=1380 ppm, has a strong impact on the recovery rate of on-the-spot ore dressing, brings huge challenge to Environmental Protection at Steel Works work.After water treatment, solve this problem preferably.From theory calculate, it is 24.84 tons according to the account form dosages of 60 times.
To water quality cyanide and adding of agent situation as table 2.
Table 2 water treatment procedure adding of agent situation
Embodiment 2: the integrated conduct method of blast furnace gas dry type bag-type dust ash
4# blast furnace dedusting ash Main Ingredients and Appearance content is as table 3.
Table 3 4# blast furnace dedusting ash Main Ingredients and Appearance content detection
Treatment process steps is:
(1) ash is unloaded: 4# blast furnace dry method ash 20 t are put into material pond and exist side by side and namely use recirculated water immersion treatment.
(2) stir: use 5t clamshell crane to grab 5 buckets and put into the agitator that diameter is 2.5m, in agitator, add water 2.2 m deeply, being configured to pulp density is 23.18 %, stirs for subsequent use after 15 minutes.
(3) ball milling: the ore pulp after stirring enters ball mill and carries out ore grinding, makes bulk lump and coarse particulate matter obtains grinding dispersion, is convenient to the ore dressing resolution ratio of follow-up flotation and gravity separation technology.
(4) flotation: ore pulp enters 4A flotation device after ball mill, according to ore pulp after mineral grain fully disperses: floating agent: diesel oil=92: the ratio of 1.08: 0.43 carries out stirring reaction, utilize 4A flotation device to carry out selecting carbon, the carbon content after flotation device flotation is 83.5%.
(5) gravity treatment: select the ore pulp after carbon to utilize the heavy physical property of iron compound to adopt spiral chute and shaking table to carry out gravity separation, the Iron concentrate obtained containing full iron 54.6% is recycled for sintering.
(6) water treatment: regularly add ferrous sulfate according to the amount of 60 times of cyanide ion concentration, total cyanogen is reduced to 12.37 below ppm.
After Filter Press, filtrate is the waste water of alkali metal containing salt, for smelting iron washing slag water.After discharge of wastewater, production system replaces salary again.
Before water treatment, system after the circulation of 32 days, potassium, sodium salt content=13.2 %, PH=12.7 in water, cyanide content=1125.3ppm.
To water quality cyanide and adding of agent situation as table 4.
Table 4 water treatment procedure adding of agent situation

Claims (1)

1. the integrated conduct method of blast furnace dry type dedusting ash, described dedusting ash main component comprises TFe=15% ~ 25%, C=14% ~ 30%, Zn=4% ~ 6%, alkali metal salt=5% ~ 7%, cyanide=0.5% ~ 1.9%, SiO 2=8% ~ 10%, Al 2o 3=2% ~ 3%, CaO+MgO=15% ~ 21%, all the other are a small amount of Pb, Cu chemical combination state or simple substance, it is characterized in that processing step is:
(1) ash is unloaded: dry method ash unloads ash and puts into material pond and exist side by side and namely use recirculated water immersion treatment;
(2) stir: add water dry method ash the mud dispersed with stirring being configured to 20% ~ 30% concentration;
(3) ball milling: the ore pulp after stirring enters ball mill grinding, makes caking and coarse particulate matter obtain grinding dispersion;
(4) flotation: according to ore pulp after mineral grain fully disperses: floating agent: diesel oil=90 ~ 100: the ratio of 1 ~ 1.2: 0.35 ~ 0.45 stirs, utilize flotation device to be sorted out by carbon wherein, what obtain carbon containing > 75% utilizes carbon;
(5) gravity treatment: select the ore pulp after carbon to adopt spiral chute and shaking table to carry out gravity separation, the Iron concentrate obtaining iron content 45% ~ 50% is recycled for sintering;
(6) water treatment: regularly add ferrous sulfate according to the amount of 50 ~ 70 times of cyanide ion concentration in water system, total cyanogen is reduced to 15 below ppm.
CN201510227331.3A 2015-05-07 2015-05-07 Comprehensive treatment method of dry reclaimed dust of blast furnace Pending CN104874583A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510227331.3A CN104874583A (en) 2015-05-07 2015-05-07 Comprehensive treatment method of dry reclaimed dust of blast furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510227331.3A CN104874583A (en) 2015-05-07 2015-05-07 Comprehensive treatment method of dry reclaimed dust of blast furnace

Publications (1)

Publication Number Publication Date
CN104874583A true CN104874583A (en) 2015-09-02

Family

ID=53942408

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510227331.3A Pending CN104874583A (en) 2015-05-07 2015-05-07 Comprehensive treatment method of dry reclaimed dust of blast furnace

Country Status (1)

Country Link
CN (1) CN104874583A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106311456A (en) * 2016-08-31 2017-01-11 蒋朋钢 Method for recovering iron concentrates and non-ferrous metals by virtue of head ash of sintering machine
CN107661813A (en) * 2016-07-29 2018-02-06 湖南隆洲驰宇科技有限公司 A kind of Comprehensive Recovery of Ag from electro-precipitating dust, lead, the method for iron
CN109265102A (en) * 2018-09-30 2019-01-25 合肥仁创铸造材料有限公司 A kind of casting dedusting ash method for innocent treatment
CN109622240A (en) * 2019-01-17 2019-04-16 山东泰东环保科技股份有限公司 A kind of flotation unit and metallurgical dedusting ash ferro element method of purification
CN111151373A (en) * 2019-06-17 2020-05-15 华北理工大学 Method for extracting carbon, iron and zinc from blast furnace cloth bag dust
CN115608517A (en) * 2021-02-05 2023-01-17 李刚强 Efficient separation method for blast furnace cloth bag dedusting ash

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1644242A (en) * 2005-01-28 2005-07-27 毛贵忠 Sorting re-utilizing process for furnace dust-proof ash
CN1699606A (en) * 2005-04-05 2005-11-23 柳州市清宇环保产业开发有限责任公司 Method for treating blast furnace dust
JP2009091189A (en) * 2007-10-09 2009-04-30 Taiheiyo Cement Corp Method and apparatus for treating gypsum board and fly ash
CN101554632A (en) * 2009-05-20 2009-10-14 重庆瑞帆再生资源开发有限公司 Harmless regeneration recycling method of trash fly ash by using blast furnace
JP2010023018A (en) * 2008-06-18 2010-02-04 Shingijutsu Kenzai Kk Pretreatment method and pretreatment device for slurried coal ash, coal ash treatment method, and coal ash treatment equipment
CN103131861A (en) * 2013-03-12 2013-06-05 山东乾舜矿冶科技股份有限公司 Integrated utilization method of ironmaking dust removal ash
CN103128097A (en) * 2013-03-22 2013-06-05 厦门大学 Processing method for incineration fly ash of municipal solid wastes
JP2013202434A (en) * 2012-03-27 2013-10-07 Taiheiyo Cement Corp Method for disposing of fluidized bed-system boiler ash and disposer
JP2013202432A (en) * 2012-03-27 2013-10-07 Taiheiyo Cement Corp Method for disposing of fluidized bed boiler ash and disposer
CN104310553A (en) * 2014-10-31 2015-01-28 武汉钢铁(集团)公司 Resource utilization method of blast furnace dust

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1644242A (en) * 2005-01-28 2005-07-27 毛贵忠 Sorting re-utilizing process for furnace dust-proof ash
CN1699606A (en) * 2005-04-05 2005-11-23 柳州市清宇环保产业开发有限责任公司 Method for treating blast furnace dust
JP2009091189A (en) * 2007-10-09 2009-04-30 Taiheiyo Cement Corp Method and apparatus for treating gypsum board and fly ash
JP2010023018A (en) * 2008-06-18 2010-02-04 Shingijutsu Kenzai Kk Pretreatment method and pretreatment device for slurried coal ash, coal ash treatment method, and coal ash treatment equipment
CN101554632A (en) * 2009-05-20 2009-10-14 重庆瑞帆再生资源开发有限公司 Harmless regeneration recycling method of trash fly ash by using blast furnace
JP2013202434A (en) * 2012-03-27 2013-10-07 Taiheiyo Cement Corp Method for disposing of fluidized bed-system boiler ash and disposer
JP2013202432A (en) * 2012-03-27 2013-10-07 Taiheiyo Cement Corp Method for disposing of fluidized bed boiler ash and disposer
CN103131861A (en) * 2013-03-12 2013-06-05 山东乾舜矿冶科技股份有限公司 Integrated utilization method of ironmaking dust removal ash
CN103128097A (en) * 2013-03-22 2013-06-05 厦门大学 Processing method for incineration fly ash of municipal solid wastes
CN104310553A (en) * 2014-10-31 2015-01-28 武汉钢铁(集团)公司 Resource utilization method of blast furnace dust

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
卢山等: "《高炉除尘灰处理技术》", 《广西节能》 *
杨逢庭等: "《高炉除尘灰的综合利用》", 《山东冶金》 *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107661813A (en) * 2016-07-29 2018-02-06 湖南隆洲驰宇科技有限公司 A kind of Comprehensive Recovery of Ag from electro-precipitating dust, lead, the method for iron
CN106311456A (en) * 2016-08-31 2017-01-11 蒋朋钢 Method for recovering iron concentrates and non-ferrous metals by virtue of head ash of sintering machine
CN109265102A (en) * 2018-09-30 2019-01-25 合肥仁创铸造材料有限公司 A kind of casting dedusting ash method for innocent treatment
CN109622240A (en) * 2019-01-17 2019-04-16 山东泰东环保科技股份有限公司 A kind of flotation unit and metallurgical dedusting ash ferro element method of purification
CN111151373A (en) * 2019-06-17 2020-05-15 华北理工大学 Method for extracting carbon, iron and zinc from blast furnace cloth bag dust
CN111151373B (en) * 2019-06-17 2022-04-08 华北理工大学 Method for extracting carbon, iron and zinc from blast furnace cloth bag dust
CN115608517A (en) * 2021-02-05 2023-01-17 李刚强 Efficient separation method for blast furnace cloth bag dedusting ash

Similar Documents

Publication Publication Date Title
CN104874583A (en) Comprehensive treatment method of dry reclaimed dust of blast furnace
CN105695735B (en) The autoreduction of a kind of steel rolling oily sludge and blast furnace dust utilizes technique
CN106498177B (en) The recycling of gold and silver iron and innoxious method is synchronized in a kind of baking cyaniding tailings
CN101914683B (en) Method for high-value and non-waste utilization of cyanidation slag
CN101451192A (en) Comprehensive recovery method for directly cyanating and intensified leaching multi-metal gold ore concentrate
CN103817015A (en) Copper and lead separating cyanide-chrome-free beneficiation method for low-grade multi-metal sulfide ore
CN111085336B (en) Method for recycling iron raw material and tail slag from rotary kiln slag without harm
CN109261347B (en) Method for resource utilization of lead-zinc smelting waste residues
CN109371233B (en) One kind heavy metal sewage sludge containing chromium and ion dust mud contaning cooperative processing method
CN108531740A (en) Process for recovering lead, zinc, carbon, silver and iron from zinc smelting leaching slag
CN101063181A (en) Rapid reduction of carbonaceous gold-containing iron ore firing residue pellet gold enrichment by using rotary hearth furnace and method for coproduction of iron powder
CN106396592A (en) Mine cemented filling material for co-processing cadmium-containing hazardous wastes and preparation method of mine cemented filling material
CN104310553B (en) The resource utilization method of blast furnace dedusting ash
CN107435102B (en) A kind of non-cyanogen leaching agent and its method for Gold ore leaching
CN104232908B (en) Method for recovering gold from gold-containing mercury smelting tailings
CN104084307A (en) Wet magnetic separation process for recycling iron in iron-containing waste
CN107460336A (en) A kind of processing method of golden cyanide residue
RU2721731C1 (en) Method of leaching and extraction of gold and silver from pyrite cinder
CN105107634A (en) Method for recovering associated sulphide copper-zinc ore from cyaniding slag of gold-silver concentrate
CN104152682A (en) Method for harmlessly treating electroplating sludge in metallurgical sintering blast furnace
CN105219972A (en) A kind of method utilizing high-carbon content flyash to reclaim iron in slag
CN117867282A (en) High-valued comprehensive utilization method and system for dust and sludge of steel plant
CN111495588B (en) Method for recycling, reducing and harmlessly treating lead-zinc smelting slag
CN101979325B (en) Refining treatment method for crude zinc oxide
CN113755693B (en) Method for co-processing roasting cyanidation tailings by utilizing acid making flue gas

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20150902