US20120180598A1 - Process using fly ash to create chunks of raw material for iron or steel mill activities. - Google Patents
Process using fly ash to create chunks of raw material for iron or steel mill activities. Download PDFInfo
- Publication number
- US20120180598A1 US20120180598A1 US13/349,782 US201213349782A US2012180598A1 US 20120180598 A1 US20120180598 A1 US 20120180598A1 US 201213349782 A US201213349782 A US 201213349782A US 2012180598 A1 US2012180598 A1 US 2012180598A1
- Authority
- US
- United States
- Prior art keywords
- agglomeration
- mixture
- waste products
- blend
- predetermined
- 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.)
- Abandoned
Links
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 title claims abstract description 46
- 238000000034 method Methods 0.000 title claims abstract description 30
- 230000008569 process Effects 0.000 title claims abstract description 27
- 229910052742 iron Inorganic materials 0.000 title claims abstract description 23
- 230000000694 effects Effects 0.000 title claims abstract description 22
- 239000010881 fly ash Substances 0.000 title claims abstract description 16
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 11
- 239000010959 steel Substances 0.000 title claims abstract description 11
- 239000002994 raw material Substances 0.000 title description 6
- 239000000203 mixture Substances 0.000 claims abstract description 55
- 238000005054 agglomeration Methods 0.000 claims abstract description 44
- 230000002776 aggregation Effects 0.000 claims abstract description 44
- 239000002699 waste material Substances 0.000 claims abstract description 32
- 238000002156 mixing Methods 0.000 claims abstract description 22
- 239000002245 particle Substances 0.000 claims abstract description 20
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 238000005266 casting Methods 0.000 claims abstract description 7
- 239000000654 additive Substances 0.000 claims abstract description 6
- 230000000996 additive effect Effects 0.000 claims abstract description 6
- 230000009467 reduction Effects 0.000 claims abstract description 6
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims description 6
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims description 3
- 239000004111 Potassium silicate Substances 0.000 claims description 3
- 239000004115 Sodium Silicate Substances 0.000 claims description 3
- YKTSYUJCYHOUJP-UHFFFAOYSA-N [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] Chemical compound [O--].[Al+3].[Al+3].[O-][Si]([O-])([O-])[O-] YKTSYUJCYHOUJP-UHFFFAOYSA-N 0.000 claims description 3
- 239000001110 calcium chloride Substances 0.000 claims description 3
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 3
- NNHHDJVEYQHLHG-UHFFFAOYSA-N potassium silicate Chemical compound [K+].[K+].[O-][Si]([O-])=O NNHHDJVEYQHLHG-UHFFFAOYSA-N 0.000 claims description 3
- 229910052913 potassium silicate Inorganic materials 0.000 claims description 3
- 235000019353 potassium silicate Nutrition 0.000 claims description 3
- 229910000029 sodium carbonate Inorganic materials 0.000 claims description 3
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 3
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 3
- 239000000047 product Substances 0.000 description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000000463 material Substances 0.000 description 5
- 239000003245 coal Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- 229920002451 polyvinyl alcohol Polymers 0.000 description 4
- 239000010802 sludge Substances 0.000 description 4
- 238000009825 accumulation Methods 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000000571 coke Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 238000009628 steelmaking Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 238000001311 chemical methods and process Methods 0.000 description 2
- 238000005520 cutting process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 238000010008 shearing Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- 239000002893 slag Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910001570 bauxite Inorganic materials 0.000 description 1
- 239000010884 boiler slag Substances 0.000 description 1
- 239000010882 bottom ash Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- JYYOBHFYCIDXHH-UHFFFAOYSA-N carbonic acid;hydrate Chemical compound O.OC(O)=O JYYOBHFYCIDXHH-UHFFFAOYSA-N 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 238000007730 finishing process Methods 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- -1 iron ore Chemical compound 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007769 metal material Substances 0.000 description 1
- 239000002923 metal particle Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/242—Binding; Briquetting ; Granulating with binders
- C22B1/243—Binding; Briquetting ; Granulating with binders inorganic
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B1/00—Preliminary treatment of ores or scrap
- C22B1/14—Agglomerating; Briquetting; Binding; Granulating
- C22B1/24—Binding; Briquetting ; Granulating
- C22B1/248—Binding; Briquetting ; Granulating of metal scrap or alloys
-
- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B7/00—Working up raw materials other than ores, e.g. scrap, to produce non-ferrous metals and compounds thereof; Methods of a general interest or applied to the winning of more than two metals
- C22B7/02—Working-up flue dust
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Definitions
- CCP Coal Combustion Products
- small particles of metallic materials are produced that are considered waste product, mainly due to the fact that it is not practical to recover these particles and re-introduce them as raw material.
- These small particles may be dust from the dust catcher of the blast furnace, scaled metal particles from finishing processes, and wet sludge from water treatment, to name a few examples. These particles are too small for reuse as raw materials in the iron making activity and are therefore hauled away and deposited in landfills.
- the present invention is directed to a chemical process of recovering waste products from an iron or steel-making activity, and a product made by the process.
- the product produced by the process sets up rapidly and in low heat situations, so that a large-sized agglomeration can be produced quickly. After set-up, the agglomeration can be divided into chunks of suitable size for use as raw material in the iron or steel-making activity.
- the inventive process helps alleviate the accumulation in the environment of Coal Combustion Products and waste products resulting from iron or steel mill activities.
- a chemical process of preparing for reuse small particles of one or more waste products produced from iron or steel mill activities, and product made thereby, having the steps and features of the present invention comprises, first creating a blend of one or more waste products with a blending system, the blend includes a predetermined proportion of each of these one or more waste products. Then, combining fly ash and the blend with a liquid in a mixing container to create a mixture. Next, adding a predetermined amount of moisture reduction additive to the mixture. Then, adjusting the amount of the liquid in the mixture to achieve a predetermined moisture and time before set up occurs. Then, mixing the mixture continuously until set up occurs and an agglomeration forms.
- the process uses the pozzolan fly ash because of fly ash's chemical characteristics, such as its rapid set up time when mixed with water and without heating.
- FIG. 1 shows the steps of an embodiment of the present invention.
- Wild Product refers to small size particles of material containing iron, carbon, alumina, magnesium, calcium or revert material such as bag-house dust, coke breeze, mill scale, bauxite fines, pellet fines, hammer mill fines, and the like.
- Set up refers to the characteristic of having been brought into a state of high plasticity.
- Iron or steel mill activity refers to metal processing activities of various types including, for example, steel making, iron making, foundry activities, and gold product manufacturing.
- a process according to the present invention of preparing for reuse small particles of one or more waste products produced from iron or steel mill activities comprises the steps of creating a blend of one or more waste products with a blending system 1 , the blend including a predetermined proportion of each of the one or more waste products; combining fly ash 4 and the blend with a liquid 3 in a mixing container to create a mixture 2 ; adding a predetermined amount of moisture reduction additive 6 to the mixture 5 ; adjusting the amount of the liquid in the mixture to achieve a predetermined moisture and time before set up occurs; mixing the mixture continuously until set up occurs and an agglomeration forms 7 ; casting the agglomeration onto a surface 8 ; dividing the agglomeration into predetermined size chunks 9 ; removing particles of less than the predetermined size from the agglomeration 10 .
- the process will necessarily produce chunks for use as raw material 11 .
- a blending system is used, such as a metering system or a bedding and blending system, to create the blend.
- the fly ash, blend and liquid water is preferred but other liquids or combinations of liquids may be appropriate, are added to a mixing unit, such as a screw mixer, drum mixer, cement mixer, pug mill mixer, paddle wheel mixer, or other similar mixer.
- a mixing unit such as a screw mixer, drum mixer, cement mixer, pug mill mixer, paddle wheel mixer, or other similar mixer.
- a moisture reduction additive In the step of adding a moisture reduction additive, an appropriate amount should be added, this is done, for example, in case the waste products are introduced with natural moisture, for instance if the waste products came from an open landfill and were subjected to rains.
- this is done to minimize the total moisture content and set up time of the mixture.
- the surface can be a conveyor system that transports the agglomeration and makes the agglomeration available for sizing.
- the agglomeration is formed into appropriately sized chunks, depending on the target mill activity, by cutting and shearing, fracturing, molding, crushing, or other similar size reducing process which reduces the size of the agglomeration.
- the fine particles that resulted primarily from dividing the agglomeration are removed by screen filtering or other similar procedure.
- the inventive process necessarily produces chunks that can be stored for later reuse or transported directly to the target mill activity location.
- a bin is at least partly filled with water treatment sludge which is of benefit to a blast furnace process because of its affect on density and chemical characteristics of an agglomeration.
- the water treatment sludge is blended at a moisture content which is required to achieve the desired chemical composition for compatibility with the blast furnace process.
- Fly ash, water, and calcium carbonate are added to the blend to create a mixture.
- the fly ash percentage changes as carbon content and oil concentration of the mixture varies in order to obtain up to a 5,000 psi final strength of the agglomeration.
- This mixture is placed in a screw mixer. Additional water or moisture reducer may be added at this point to regulate a total moisture content and affect the set up time of the mixture.
- agglomeration of fly ash, water, and sludge.
- the agglomeration is then discharged onto a moving belt.
- the agglomeration is cut and sheared into 2.5 inch chunks before the agglomeration cures.
- the agglomeration chunks are then screened to eliminate undesirable fines that result from the cutting and shearing.
- the resulting chunks are then moved to storage or directly to a recycling unit.
- a curing accelerator can be added to the process if it is desirable to decrease the time to cure.
- a curing accelerator will be one selected from the group consisting of sodium carbonate, sodium silicate, calcium chloride, potassium silicate and aluminum silicate. Therefore, the spirit and scope of the appended claims should not be limited to the description of the preferred versions contained herein.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Geology (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Environmental & Geological Engineering (AREA)
- Materials Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Geochemistry & Mineralogy (AREA)
- Inorganic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
A process of preparing for reuse small particles of one or more waste products produced from iron or steel mill activities, comprising the steps of creating a blend of one or more waste products with a blending system, the blend including a predetermined proportion of each of the one or more waste products, combining fly ash and the blend with a liquid in a mixing container to create a mixture, adding a predetermined amount of moisture reduction additive to the mixture, adjusting the amount of the liquid in the mixture to achieve a predetermined moisture and time before set up occurs, mixing the mixture continuously until set up occurs and an agglomeration forms, casting the agglomeration onto a surface, dividing the agglomeration into predetermined size chunks, removing particles of less than the predetermined size from the agglomeration. The chunks produced according to this process.
Description
- This application claims the benefit of U.S. Provisional Application No. 61/432,478, filed Jan. 13, 2011.
- Many iron and steel mill activities have negative environmental impact. Mills have waste generating activities that create problems related to landfills, air and water pollution. These streams of waste present problems for which a solution is necessary. Combustion of coal produces several distinct byproducts referred to as Coal Combustion Products (“CCP”). These CCPs include fly ash, bottom ash, and boiler slag. Several million tons of these CCPs are disposed of in landfills every year, which only adds to the negative environmental impact that iron and steel mills already impose.
- When making iron, raw materials like iron ore, coke and limestone are mixed and heated in a blast furnace. There, carbon monoxide produced from the burning coke reduces the iron ore to iron. Gangue in the iron ore reacts with the limestone to produce slag. The slag is often removed as a waste product of the iron making activity and transported for further processing which creates fine material that is then moved to a landfill.
- Also during the iron making activity, small particles of metallic materials are produced that are considered waste product, mainly due to the fact that it is not practical to recover these particles and re-introduce them as raw material. These small particles may be dust from the dust catcher of the blast furnace, scaled metal particles from finishing processes, and wet sludge from water treatment, to name a few examples. These particles are too small for reuse as raw materials in the iron making activity and are therefore hauled away and deposited in landfills.
- Attempts have been made to develop methods of grouping together these small particles into larger-sized pieces that could then, in the case of a blast furnace, be dumped into the top of the blast furnace for reuse. For example, sintering and briquetting have both been utilized to try to fashion usable pieces of material from the small particles. These attempts have, thus far proved to be economically or otherwise unfeasible for various reasons. Sintering, for example, creates stack emission air polluting problems due to the burning of the particles. Briquetting, as another example, requires dry and uniformly sized materials, and so requires additional process steps to achieve these requirements.
- Information relevant to attempts to address these problems can be found in U.S. Pat. Nos. 5,556,457 (Terza) and 5,395,441 (Bogdan). However, each one of these references suffers minimally from one or more of the following disadvantages: 1) set up time of the resultant product is too long, 2) high temperature is required for set up, 3) these solutions do nothing to alleviate the accumulation of CCPs, such as fly ash, in the world's landfills.
- For the foregoing reasons, there is a need in the industry for a process that produces a product that sets up rapidly and in low heat situations, and helps alleviate the accumulation of Coal Combustion Products and waste products from iron or steel mill activities in the environment.
- The present invention is directed to a chemical process of recovering waste products from an iron or steel-making activity, and a product made by the process. The product produced by the process sets up rapidly and in low heat situations, so that a large-sized agglomeration can be produced quickly. After set-up, the agglomeration can be divided into chunks of suitable size for use as raw material in the iron or steel-making activity. The inventive process helps alleviate the accumulation in the environment of Coal Combustion Products and waste products resulting from iron or steel mill activities.
- A chemical process of preparing for reuse small particles of one or more waste products produced from iron or steel mill activities, and product made thereby, having the steps and features of the present invention comprises, first creating a blend of one or more waste products with a blending system, the blend includes a predetermined proportion of each of these one or more waste products. Then, combining fly ash and the blend with a liquid in a mixing container to create a mixture. Next, adding a predetermined amount of moisture reduction additive to the mixture. Then, adjusting the amount of the liquid in the mixture to achieve a predetermined moisture and time before set up occurs. Then, mixing the mixture continuously until set up occurs and an agglomeration forms. Then, casting the agglomeration onto a surface and then dividing the agglomeration into predetermined size chunks. Next, removing particles of less than the predetermined size from the agglomeration. The foregoing process will result in a product that can be used as charge in a blast furnace, for example.
- Importantly, the process uses the pozzolan fly ash because of fly ash's chemical characteristics, such as its rapid set up time when mixed with water and without heating.
- These and other features, aspects and advantages of the present invention will become better understood with regard to the following description, appended claims, and accompanying drawing where
FIG. 1 shows the steps of an embodiment of the present invention. - Definitions.
- “Waste Product” refers to small size particles of material containing iron, carbon, alumina, magnesium, calcium or revert material such as bag-house dust, coke breeze, mill scale, bauxite fines, pellet fines, hammer mill fines, and the like. “Set up” refers to the characteristic of having been brought into a state of high plasticity. “Iron or steel mill activity” refers to metal processing activities of various types including, for example, steel making, iron making, foundry activities, and gold product manufacturing.
- Overview.
- As shown in
FIG. 1 , a process according to the present invention of preparing for reuse small particles of one or more waste products produced from iron or steel mill activities, comprises the steps of creating a blend of one or more waste products with ablending system 1, the blend including a predetermined proportion of each of the one or more waste products; combiningfly ash 4 and the blend with aliquid 3 in a mixing container to create amixture 2; adding a predetermined amount ofmoisture reduction additive 6 to themixture 5; adjusting the amount of the liquid in the mixture to achieve a predetermined moisture and time before set up occurs; mixing the mixture continuously until set up occurs and anagglomeration forms 7; casting the agglomeration onto asurface 8; dividing the agglomeration into predeterminedsize chunks 9; removing particles of less than the predetermined size from theagglomeration 10. The process will necessarily produce chunks for use asraw material 11. - In the step of creating a blend, a blending system is used, such as a metering system or a bedding and blending system, to create the blend.
- In the step of combining fly ash and the blend with a liquid, the fly ash, blend and liquid, water is preferred but other liquids or combinations of liquids may be appropriate, are added to a mixing unit, such as a screw mixer, drum mixer, cement mixer, pug mill mixer, paddle wheel mixer, or other similar mixer.
- In the step of adding a moisture reduction additive, an appropriate amount should be added, this is done, for example, in case the waste products are introduced with natural moisture, for instance if the waste products came from an open landfill and were subjected to rains.
- In the step of adjusting the amount of the liquid, this is done to minimize the total moisture content and set up time of the mixture.
- In the step of mixing the mixture, continuous agitation is applied to the mixture by the mixer for approximately 10 minutes.
- In the step of casting the agglomeration onto a surface, the surface can be a conveyor system that transports the agglomeration and makes the agglomeration available for sizing.
- In the step of dividing the agglomeration, the agglomeration is formed into appropriately sized chunks, depending on the target mill activity, by cutting and shearing, fracturing, molding, crushing, or other similar size reducing process which reduces the size of the agglomeration.
- In the step of removing particles, the fine particles that resulted primarily from dividing the agglomeration are removed by screen filtering or other similar procedure.
- The inventive process necessarily produces chunks that can be stored for later reuse or transported directly to the target mill activity location.
- A bin is at least partly filled with water treatment sludge which is of benefit to a blast furnace process because of its affect on density and chemical characteristics of an agglomeration. The water treatment sludge is blended at a moisture content which is required to achieve the desired chemical composition for compatibility with the blast furnace process. Fly ash, water, and calcium carbonate are added to the blend to create a mixture. The fly ash percentage changes as carbon content and oil concentration of the mixture varies in order to obtain up to a 5,000 psi final strength of the agglomeration. This mixture is placed in a screw mixer. Additional water or moisture reducer may be added at this point to regulate a total moisture content and affect the set up time of the mixture. Mixing is carried out for about 10 minutes creating an agglomeration of fly ash, water, and sludge. The agglomeration is then discharged onto a moving belt. The agglomeration is cut and sheared into 2.5 inch chunks before the agglomeration cures. The agglomeration chunks are then screened to eliminate undesirable fines that result from the cutting and shearing. The resulting chunks are then moved to storage or directly to a recycling unit.
- Although the present invention has been described in considerable detail with the reference to certain preferred versions thereof, other versions are possible. For example, there can be a plurality of waste products used, not just a single waste product. Or a curing accelerator can be added to the process if it is desirable to decrease the time to cure. Such a curing accelerator will be one selected from the group consisting of sodium carbonate, sodium silicate, calcium chloride, potassium silicate and aluminum silicate. Therefore, the spirit and scope of the appended claims should not be limited to the description of the preferred versions contained herein.
Claims (7)
1. A process for converting small particles of one or more reusable waste products into an agglomeration, the one or more reusable waste products being produced from iron or steel mill activities, the process comprising:
(a) creating a blend of one or more waste products with a blending system, the blend including a predetermined proportion of each of the one or more waste products;
(b) combining fly ash and the blend with a liquid in a mixing container to create a mixture;
(c) adding a predetermined amount of moisture reduction additive to the mixture;
(d) adjusting an amount of the liquid in the mixture to achieve a predetermined moisture and time before set up occurs;
(e) mixing the mixture continuously until set up occurs and an agglomeration forms;
(f) casting the agglomeration onto a surface;
(g) dividing the agglomeration into predetermined size chunks;
(h) removing particles of less than the predetermined size from the agglomeration.
2. The process according to claim 1 further comprising:
(a) adding a curing accelerator to the mixture prior to forming the agglomeration, the curing accelerator being selected from the group consisting of sodium carbonate, sodium silicate, calcium chloride, potassium silicate and aluminum silicate.
3. The chunks produced according to the process of claim 1 .
4. A process for converting small particles of one or more reusable waste products into an agglomeration, the one or more reusable waste products being produced from iron or steel mill activities, the process comprising:
(b) creating a blend of one or more waste products with a blending system, the blend including a predetermined proportion of each of the one or more waste products;
(c) combining fly ash and the blend with a liquid in a mixing container to create a mixture;
(d) adding a predetermined amount of moisture reduction additive to the mixture;
(e) adjusting an amount of the liquid in the mixture to achieve a predetermined moisture and time before set up occurs;
(f) adding a curing accelerator to the mixture prior to forming the agglomeration, the curing accelerator being selected from the group consisting of sodium carbonate, sodium silicate, calcium chloride, potassium silicate and aluminum silicate.
(g) mixing the mixture continuously until set up occurs and an agglomeration forms;
(h) casting the agglomeration onto a surface;
(i) dividing the agglomeration into predetermined size chunks;
(j) removing particles of less than the predetermined size from the agglomeration.
5. The chunks produced according to the process of claim 4 .
6. A process for converting small particles of one or more reusable waste products into an agglomeration, the one or more reusable waste products being produced by a metal-processing activity, the process comprising:
(a) measuring a first amount and a second amount of a first and second reusable waste product, respectively;
(b) blending the first amount and the second amount together to produce a uniform mixture;
(c) adding fly ash and liquid to the mixture;
(d) mixing the mixture continuously until the mixture starts to set-up;
(e) casting the mixture onto a surface to form an agglomeration; and
(f) after the agglomeration sets-up, divide the agglomeration into pieces sized for reintroduction into the metal-making activity.
7. The pieces produced according to the process of claim 6 .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US13/349,782 US20120180598A1 (en) | 2011-01-13 | 2012-01-13 | Process using fly ash to create chunks of raw material for iron or steel mill activities. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201161432478P | 2011-01-13 | 2011-01-13 | |
| US13/349,782 US20120180598A1 (en) | 2011-01-13 | 2012-01-13 | Process using fly ash to create chunks of raw material for iron or steel mill activities. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20120180598A1 true US20120180598A1 (en) | 2012-07-19 |
Family
ID=46489726
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US13/349,782 Abandoned US20120180598A1 (en) | 2011-01-13 | 2012-01-13 | Process using fly ash to create chunks of raw material for iron or steel mill activities. |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US20120180598A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20190308909A1 (en) * | 2016-05-10 | 2019-10-10 | Bmm Ventures, Llc | Sintered ceramics |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5885328A (en) * | 1996-05-31 | 1999-03-23 | Ltv Steel Company, Inc. | Method of agglomerating oil-containing steel mill waste |
-
2012
- 2012-01-13 US US13/349,782 patent/US20120180598A1/en not_active Abandoned
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5885328A (en) * | 1996-05-31 | 1999-03-23 | Ltv Steel Company, Inc. | Method of agglomerating oil-containing steel mill waste |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20190308909A1 (en) * | 2016-05-10 | 2019-10-10 | Bmm Ventures, Llc | Sintered ceramics |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2224007C1 (en) | Elevated-strength coal briquette and a method of fabrication thereof | |
| EP0861909B1 (en) | Use of a briquette of foundry waste agglomerated with a hydraulic binder as a charge material for smelting furnaces of an iron foundry | |
| RU2264435C2 (en) | Coal briquettes for reductive melting process and a method for manufacture thereof | |
| EP1579016B1 (en) | Cold briquetting and pelletisation of mineral fines using an iron-bearing hydraulic binder | |
| US6921427B2 (en) | Process for cold briquetting and pelletization of ferrous or non-ferrous ores or mineral fines by iron bearing hydraulic mineral binder | |
| WO2019033187A1 (en) | Process of cold pelletization of iron-ore fines with mixture flexibility | |
| US4465520A (en) | Method and apparatus for the removal of objectionable volatile compounds from hot gases | |
| JP4927702B2 (en) | Process for producing mixed raw materials for sintering | |
| US20120180598A1 (en) | Process using fly ash to create chunks of raw material for iron or steel mill activities. | |
| RU2619427C2 (en) | Titanium-containing charge for titanium tetrachloride production and method of its preparation | |
| WO2007080356A1 (en) | Production of carbonaceous metal ore pellets | |
| JPS63500237A (en) | Method for converting organic and inorganic wastes into solid inert water-insoluble substances | |
| CN104907532A (en) | Chromium slag harmlessness processing method by taking tailings and chromium slag as sintering fusing agents after steel slag magnetic separation | |
| CN104099467A (en) | Technology for producing regenerated, cured and formed manganese ore blocks by using manganese-silicon alloy smelting industrial fumes | |
| KR20090125511A (en) | Binder and its manufacturing method | |
| AU719637B2 (en) | Reuse of metallurgical fines | |
| RU2853225C1 (en) | Method for processing technogenic gypsum into anhydrite for use in backfill mixture | |
| JP5861453B2 (en) | Agglomeration method and recycling method of shredder dust | |
| JP5200422B2 (en) | Hot metal production method using vertical scrap melting furnace | |
| JP2008291331A (en) | Method for producing zinc-containing dust agglomerates | |
| JP2021155306A (en) | Manufacturing method of clinker fine aggregate, and manufacturing method of cement clinker | |
| KR100952224B1 (en) | Non-fired pellet manufacturing method using wire rod sludge | |
| Nezamaev et al. | Technological peculiarities of phosphate pellets production stages from concentrate and ore raw materials | |
| SU1708891A1 (en) | Method of production of fluxed sinter | |
| GB2521021A (en) | Method of treating hot mill iron-containing sludge from iron and steel making processes |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |