US20080005956A1 - Methods and compositions for controlling bulk density of coking coal - Google Patents

Methods and compositions for controlling bulk density of coking coal Download PDF

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Publication number
US20080005956A1
US20080005956A1 US11/857,093 US85709307A US2008005956A1 US 20080005956 A1 US20080005956 A1 US 20080005956A1 US 85709307 A US85709307 A US 85709307A US 2008005956 A1 US2008005956 A1 US 2008005956A1
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United States
Prior art keywords
weight percent
fatty acid
treating composition
coal
bulk density
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
Application number
US11/857,093
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English (en)
Inventor
Bo Tran
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.)
Ecolab USA Inc
Original Assignee
Nalco Co LLC
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
Priority claimed from US10/846,218 external-priority patent/US7108800B2/en
Priority claimed from US11/490,193 external-priority patent/US7398935B2/en
Priority claimed from US11/561,150 external-priority patent/US20080115409A1/en
Application filed by Nalco Co LLC filed Critical Nalco Co LLC
Priority to US11/857,093 priority Critical patent/US20080005956A1/en
Assigned to NALCO COMPANY reassignment NALCO COMPANY ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: TRAN, BO L.
Publication of US20080005956A1 publication Critical patent/US20080005956A1/en
Priority to TW097130469A priority patent/TW200914602A/zh
Priority to EP12151673A priority patent/EP2479240A1/en
Priority to CA2698391A priority patent/CA2698391C/en
Priority to PCT/US2008/076476 priority patent/WO2009039070A2/en
Priority to JP2010525076A priority patent/JP2010539298A/ja
Priority to AU2008302481A priority patent/AU2008302481B2/en
Priority to CL2008002774A priority patent/CL2008002774A1/es
Priority to CN200880107264.XA priority patent/CN101802133B/zh
Priority to BRPI0815519-4A priority patent/BRPI0815519B1/pt
Priority to MX2010002798A priority patent/MX2010002798A/es
Priority to EP08799561A priority patent/EP2193180A2/en
Priority to US12/356,352 priority patent/US20090127499A1/en
Assigned to BANK OF AMERICA, N.A., AS COLLATERAL AGENT reassignment BANK OF AMERICA, N.A., AS COLLATERAL AGENT SECURITY AGREEMENT Assignors: CALGON LLC, NALCO COMPANY, NALCO CROSSBOW WATER LLC, NALCO ONE SOURCE LLC
Assigned to NALCO CMPANY reassignment NALCO CMPANY CORRECTIVE ASSIGNMENT TO CORRECT THE ADD ADITIONAL INVENTOR TO ASSIGNMENT PREVIOUSLY RECORDED ON REEL 019842 FRAME 0721. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Assignors: TRAN, BO L., HAMNIK, JOSEPH M.
Priority to ZA2010/01784A priority patent/ZA201001784B/en
Assigned to NALCO COMPANY reassignment NALCO COMPANY RELEASE BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: BANK OF AMERICA, N.A.
Assigned to NALCO COMPANY reassignment NALCO COMPANY RELEASE BY SECURED PARTY (SEE DOCUMENT FOR DETAILS). Assignors: BANK OF AMERICA, N.A.
Assigned to ECOLAB USA INC. reassignment ECOLAB USA INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: CALGON CORPORATION, CALGON LLC, NALCO COMPANY LLC, ONDEO NALCO ENERGY SERVICES, L.P.
Assigned to NALCO COMPANY LLC reassignment NALCO COMPANY LLC CHANGE OF NAME (SEE DOCUMENT FOR DETAILS). Assignors: NALCO COMPANY
Assigned to ECOLAB USA INC. reassignment ECOLAB USA INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: NALCO COMPANY
Abandoned legal-status Critical Current

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L9/00—Treating solid fuels to improve their combustion
    • C10L9/10—Treating solid fuels to improve their combustion by using additives
    • C10L9/12—Oxidation means, e.g. oxygen-generating compounds
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/10—Biofuels, e.g. bio-diesel
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel

Definitions

  • This invention relates to controlling the bulk density of coking coal. More particularly, this invention concerns compositions to control coal bulk density comprising liquid hydrocarbons derived from biomass.
  • the biomass liquid hydrocarbons can include vegetable oils, animal fats, triglycerides, fatty acids, fatty acid methyl esters, fatty acid ethyl esters, and glycerin.
  • the liquid hydrocarbon is applied on the coking coal to adjust the coal's bulk density.
  • Metallurgical coke is prepared by heating coal in an oxygen-free atmosphere until all the volatile components in the coal evaporate.
  • Metallurgical coal is mainly used in the iron and steel industry as fuel for blast furnaces, sinter plants, and foundries to reduce iron ore to iron.
  • the coking of coal occurs in coke ovens without contact with air in ovens that are designed to operate at optimum wall pressure. During operation the oven is subjected to cyclic stress of expansion and contraction. It is essential that the bulk density of coal is measured and controlled to prevent excessive pressure within the ovens and to run the ovens at optimum capacity.
  • Raw coking coals rarely possess the requisite bulk density, primarily due to the presence of surface moisture on the coal. Surface moisture decreases the bulk density of formerly dry coking coal.
  • a widely used procedure is to apply diesel fuel to the coal. The fuel increases the coal's bulk density and thereby controls expansion that can damage the oven.
  • Diesel fuel is derived from petroleum hydrocarbons and emits pollutants during the coking process. Its cost has also escalated recently. It is therefore desirable to identify compositions for adjusting the bulk density of coal that are derived from renewable sources, that emit less pollution, are less hazardous to human health and the environment and are cost effective.
  • This invention concerns methods and compositions to control the bulk density of coking coal.
  • this invention is a method of adjusting the bulk density of coking coal comprising applying to the coal an effective bulk density increasing amount of a treating composition comprising about 10 to about 99 weight percent of one or more components selected from a group consisting of vegetable oils, animal fats, triglycerides, fatty acids, fatty acid methyl esters, fatty acid ethyl esters, and glycerin.
  • compositions according to this invention can be used in place of diesel fuel or contain substantially reduced amounts of diesel fuel.
  • the compositions are derived from renewable resources and comprise green chemistries.
  • the compositions can comprise by-products of biodiesel manufacturing processes and of soap and detergent manufacturing processes. This makes using them cost effective.
  • pollutant emissions including total unburned hydrocarbons, carbon monoxide, particulate, sulfates, polyaromatic hydrocarbons (PAH), and nitrated PAH, may be lower than when diesel fuel is used to adjust the bulk density during the coking process.
  • compositions can reduce moisture content of the coal consequently, improving its through put characteristics.
  • compositions comprising biomass liquids such as vegetable oils, animal fats, triglycerides, fatty acids, fatty acid methyl esters, fatty acid ethyl esters, and glycerin.
  • biomass liquids such as vegetable oils, animal fats, triglycerides, fatty acids, fatty acid methyl esters, fatty acid ethyl esters, and glycerin.
  • the vegetable oils, animal fats, triglycerides, fatty acids, fatty acid methyl esters, fatty acid ethyl esters, and glycerin described herein are “green”, i.e., non-hazardous, non-toxic, biodegradable, environmentally friendly, and derived from renewable sources.
  • Triglycerides refer to esters of glycerol a trihydric alcohol, with different fatty acids of varying molecular weigh associated with a particular oil or fat. Triglycerides are the principle components of fats, tallow oil, yellow grease, and/or vegetable oils. The most common fatty acids sourced from natural fats and oils include palmitic, stearic and linoleic acid.
  • “Fatty acids” means carboxylic acids derived from or contained in an animal or vegetable fat or oil. Fatty acids comprise a terminal COOH group and a long chain saturated or unsaturated alkyl chain. Representative fatty acids include butyric acid, lauric acid, palmitic acid, stearic acid, oleic acid, linoleic acid, linolenic acid, and the like.
  • Glycerin and “glycerol” means 1,2,3-propanetriol.
  • Glycerin, fatty acids, fatty acid methyl esters, and/or fatty acid ethyl esters can be derived as by-products from transesterification reactions involving triglycerides including transesterification reactions involving biodiesel manufacturing processes as described herein.
  • “Vegetable oil” means triglycerides extracted from the seeds, fruit or leaves of plants including corn oil, soybean oil, canola oil, palm oil, coconut oil, rapeseed oil, and the like.
  • Diesel fuel includes fuel oil #1 and fuel oil #2 and the like.
  • Transesterification reactions involving triglycerides refers to the splitting of triglyceride esters derived from vegetable oils and/or animal fats in the presence of base and a monohydroxy alcohol such as methanol or ethanol to produce monoesters of the fatty acids comprising the original triglycerides.
  • “Surfactant” is any substance used to lower the surface tension of another substance. In an embodiment the present invention is used with a surfactant to improve the coal bulk density and to improve the flow characteristic of coal.
  • the methyl esters, ethyl esters, glycerin and fatty acids are derived from transesterification reactions involving triglycerides.
  • Representative fats and oils used in the transesterification reactions described herein include tallow, crude tall oil, virgin vegetable oils, soy, mustard, canola, coconut, rapeseed, palm, poultry offal, fish oils, yellow grease, used cooking oils, and/or trap grease, and the like.
  • the glycerin, fatty acids, ethyl esters and methyl esters are derived from a biodiesel manufacturing process.
  • Biodiesel is a cleaner-burning diesel replacement fuel made from natural, renewable sources.
  • biodiesel can include fatty acid alkyl esters used as a cleaner-burning diesel replacement fuel made from sources such as new and used vegetable oils and animal fats.
  • Biodiesel is typically made through a chemical process called transesterification in which vegetable oil or animal fats are converted to fatty acid alkyl esters and glycerin by-products.
  • Fatty acids and fatty acid alkyl esters can be produced from oils and fats by base-catalyzed transesterification of the oil, direct acid-catalyzed esterification of the oil and conversion of the oil to fatty acids and subsequent esterification to biodiesel.
  • fatty acid alkyl esters are produced by the base-catalyzed method.
  • any base may be used as the catalyst used for transesterification of the oil to produce biodiesel, however sodium hydroxide or potassium hydroxide are used in most commercial processes.
  • the oils and fats can be filtered and preprocessed to remove water and contaminants. If free fatty acids are present, they can be removed or transformed into biodiesel using special pretreatment technologies, such as acid catalyzed esterification.
  • the pretreated oils and fats can then be mixed with an alcohol and a catalyst (e.g. base).
  • the base used for the reaction is typically sodium hydroxide or potassium hydroxide, being dissolved in the alcohol used (typically ethanol or methanol) to form the corresponding alkoxide, with standard agitation or mixing. It should be appreciated that any suitable base can be used.
  • the alkoxide may then be charged into a closed reaction vessel and the oils and fats are added. The system can then be closed, and held at about 71° C. (160° F.) for a period of about 1 to 8 hours, although some systems recommend that the reactions take place at room temperature.
  • oil molecules e.g. triglycerides
  • two major products are produced: 1) a crude fatty acid alkyl esters phase (i.e. biodiesel phase) and 2) a glycerin by-product phase.
  • the crude fatty acid alkyl esters phase forms a layer on top of the denser glycerin by-product phase.
  • the glycerin by-product phase is denser than the biodiesel phase, the two can be gravity separated.
  • the glycerin by-product phase can be simply drawn off the bottom of a settling vessel. In some cases, a centrifuge may be employed to speed the separation of the two phases.
  • the glycerin by-product phase typically consists of a mixture of glycerin, methyl esters, methanol, mong and inorganic salts and water.
  • Mong is “matiere organique non glycerol”.
  • Mong normally consists of soaps, free fatty acids, and other impurities.
  • Methyl esters or ethyl esters are typically present in an amount of about 0.01 to about 5 percent by weight.
  • Methanol can be present in the glycerin by-product in an amount from about 0.1 weight. percent to about 35 weight percent
  • the glycerin-containing by-product may comprise about 30 to about 95 weight percent of glycerin. In certain instances, it may be necessary to further refine the glycerin by-product prior to use, for example by washing, acidulation or distillation to adjust the glycerin concentration and/or remove impurities.
  • the fatty acid by-products can originate from the refining of the crude fatty acid alkyl esters phase and/or the crude glycerin phase during the biodiesel manufacturing process.
  • the crude fatty acid alkyl esters phase typically includes a mixture of fatty acid alkyl esters, water and a fatty acid salts component.
  • These fatty acid salts component generally form a solution with the water phase (e.g. soap water) where they can be further separated from the fatty acid alkyl esters component.
  • any suitable acid such as, for example, hydrochloric acid can be added to the water phase containing the fatty acid salts component to produce the fatty acid by-products of the present invention.
  • the fatty acid by-product may be in a wax or solid form. It can also contain fatty acid esters.
  • the esters are beneficial components of this invention.
  • the methyl esters or ethyl esters are sometime concentrated through further processing, including washing or distilling.
  • the methyl or ethyl ester by-products can contain other components, including triglycerides, diglycerides, monoglycerides, sterol, fatty acids, tocopherol, and other impurities.
  • the crude glycerin phase typically includes a mixture of glycerin, water and a fatty acid salts component.
  • This fatty acid salts component forms a solution or suspension with the water phase where it can be further separated from the glycerin component by adding any suitable acid to recover the fatty acid by-products suitable for the present invention.
  • the fatty acid by-products of the present invention can be derived from the acidulation of any of the biodiesel manufacturing process streams/stages that contain the fatty acid salts component (e.g. soap water) including, for example, the wash water.
  • the fatty acid salts component e.g. soap water
  • These fatty acid by-products derived from any of the different stages/streams of the biodiesel manufacturing process can be used as compositions to adjust the bulk density of coal.
  • Coke production from coal occurs in ovens absence of air. These ovens are airtight while in operation and are subjected to cyclic stress of expansion and contraction. Each oven consists of three areas: coking chambers, heating chambers, and regenerative chambers. All the chambers are lined with refractory brick. The coking chambers have ports on the top for charging the coal.
  • Coke manufacturing consists of preparing, charging, and heating the coal; removing and cooling the coke product; and cooling, cleaning, and recycling the oven gas. Approximately 40 percent of cleaned oven gas (after the removal of its by-products) is used to heat the coke ovens.
  • Preparation of the coal for coking involves pulverization to induce transfer through a 3.2 millimeter screen.
  • Several types of coal can be blended to produce the desired properties, or to control expansion of the coal mixture in the oven.
  • Water or oil, including diesel fuel, may be added to the coal to adjust its density. The purpose is to control expansion, preventing damage to the oven.
  • Coal is added to the ovens dry or wet. Wall temperatures are about 2000 degree F. during loading and actual coking. The ports are closed after the coal is charged, and the coal is heated for about 12 to 20 hours.
  • Air pollutants including particulates, volatile organic compounds, carbon monoxide, and other compounds are emitted from the different coking operation, i.e., coal preparation, coal preheating, coal charging, oven leakage, coke removal, hot coke quenching, and combustion stacks.
  • This invention uses novel treating compositions comprising biomass liquids derived from renewable resources to adjust the bulk density of coal.
  • the invention uses compositions that are green, emit less pollutants, and are cost-effective.
  • the treating composition comprises one or more fatty acid methyl esters, fatty acid ethyl esters or a combination thereof for adjusting the bulk density of coal.
  • fatty acid methyl and ethyl esters are also known as biodiesel, and have been used to replace diesel fuel for use in vehicle engines and in boilers. Emissions from these applications are reportedly less when biodiesel is used in place of diesel fuel.
  • the National Biodiesel Board reports reduction of total unburned hydrocarbons by 67%, reduction of carbon monoxide by 48%, reduction of particulate matter by 47%, reduction of sulfates by 100%, reduction of polyaromatic hydrocarbons by 80%, reduction of nitrated PAHs by 90%, and reduction of ozone potential of speciated hydrocarbon by 50%.
  • the treating composition comprises from about 30 to about 99 weight percent fatty acid methyl esters, fatty acid ethyl esters or a combination thereof
  • the treating composition comprises about 40 to about 85 weight percent of fatty acid methyl esters, about 3 to about 50 weight percent fatty acids, about 0.5 to about 5 weight percent tocopherols, and about 0.5 to about 5 weight percent of sterols.
  • the treating composition comprises from about 10 to about 99 weight percent glycerin.
  • the treating composition comprises about 95 to about 99 weight percent of glycerin, about 0.05 to about 1 weight percent methanol, and about 0.05 to about 1 weight percent water.
  • the treating composition further comprises diesel fuel.
  • the treating composition comprises about 30 to about 70 weight percent diesel fuel.
  • diesel fuel can be applied to coal to adjust the coal bulk density and compensate for surface moisture on the coal. Accordingly, in an embodiment, the treating composition further comprises diesel fuel.
  • the treating composition comprises about 30 percent by weight to about 70 percent by weight diesel fuel.
  • the treating composition comprises about 30 to about 99.9 weight percent fatty acid methyl esters and about 0.1 to about 70 weight percent diesel fuel.
  • One or more surfactants may be added to the treating composition in order to increase the spreading coefficient of the components.
  • Surfactants may be oil soluble or water soluble depending whether the treating composition is aqueous or nonaqueous.
  • Representative surfactants including long chain primary and secondary alcohols, linear alcohols, akylaryl sulfonates and mixtures thereof should be used for nonaqueous treating compositions.
  • one or more C 1 -C 8 alcohols may advantageously be included in the treating composition.
  • Representative C 1 -C 8 alcohols include methanol, ethanol, isopropanol, octanol, and the like.
  • the treating composition comprises about 5 to about 30 weight percent surfactants, about 70 to about 95 weight percent fatty acid methyl esters and about 0.1 to about 25 weight percent diesel fuel.
  • the treating composition may be sprayed, poured, or otherwise applied to the coal at any stage before the coal is placed in the coking oven.
  • the amount of treating composition required per ton of coal to achieve the desired increase in bulk density can be empirically determined by one of skill in the art taking into consideration the type of coal being treated and its surface moisture content. In an embodiment about 1 to about 20 pints of said treating composition per ton of coal is applied to the coal.
  • Crude glycerin solution is obtained from a biodiesel synthesis process.
  • the crude glycerin component comprises about 80 weight percent of glycerin, about 10-11 weight percent of water, about 7 weight percent of sodium chloride, and about 1-2 weight percent of fatty acids and methyl esters thereof.
  • the product is diluted with 42 weight percent of water to provide a 58 weight percent solution of the crude glycerin byproduct.
  • the composition is applied to coal at 2 pints per ton (ppt). Two samples were created: one with the treated coal; and one without the glycerin treatment. No. 2 fuel oil was then added to both samples at identical oil concentration. At the oil concentration range of 4 ppt, the sample treated with glycerin exhibited a higher bulk density of about 1 lb per cubic foot.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Liquid Carbonaceous Fuels (AREA)
  • Fats And Perfumes (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)
  • Coke Industry (AREA)
US11/857,093 2004-05-14 2007-09-18 Methods and compositions for controlling bulk density of coking coal Abandoned US20080005956A1 (en)

Priority Applications (14)

Application Number Priority Date Filing Date Title
US11/857,093 US20080005956A1 (en) 2004-05-14 2007-09-18 Methods and compositions for controlling bulk density of coking coal
TW097130469A TW200914602A (en) 2007-09-18 2008-08-11 Methods and compositions for controlling bulk density of coking coal
EP08799561A EP2193180A2 (en) 2007-09-18 2008-09-16 Methods and compositions for controlling bulk density of coking coal
MX2010002798A MX2010002798A (es) 2007-09-18 2008-09-16 Metodos y composiciones para controlar la densidad a granel de carbon mineral para coquizado.
EP12151673A EP2479240A1 (en) 2007-09-18 2008-09-16 Methods and compositions for controlling bulk density of coking coal
BRPI0815519-4A BRPI0815519B1 (pt) 2007-09-18 2008-09-16 "método para ajustar a densidade nominal do coque de carvão"
CN200880107264.XA CN101802133B (zh) 2007-09-18 2008-09-16 用于控制焦煤的堆密度的方法和组合物
CL2008002774A CL2008002774A1 (es) 2007-09-18 2008-09-16 Metodo para ajustar la densidad aparente del carbon coque; y composiciones de tratamiento para mejorar la densidad aparente y las propiedades de rendimiento del carbon coque.
CA2698391A CA2698391C (en) 2007-09-18 2008-09-16 Methods and compositions for controlling bulk density of coking coal
PCT/US2008/076476 WO2009039070A2 (en) 2007-09-18 2008-09-16 Methods and compositions for controlling bulk density of coking coal
JP2010525076A JP2010539298A (ja) 2007-09-18 2008-09-16 粘結炭の嵩密度を制御するための方法及び組成物
AU2008302481A AU2008302481B2 (en) 2007-09-18 2008-09-16 Methods and compositions for controlling bulk density of coking coal
US12/356,352 US20090127499A1 (en) 2004-05-14 2009-01-20 Methods and compositions for dust control and freeze conditioning
ZA2010/01784A ZA201001784B (en) 2007-09-18 2010-03-11 Methods and composition for controlling bulk density of coking coal

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
US10/846,218 US7108800B2 (en) 2004-05-14 2004-05-14 Method for preventing the agglomeration or generation of dust from a particulate material comprising coal
US11/490,193 US7398935B2 (en) 2004-05-14 2006-07-20 Methods and compositions for dust control and freeze control
US11/561,150 US20080115409A1 (en) 2006-11-17 2006-11-17 Alternative fuel comprising combustible solids and by-products or waste material from industrial processes
US11/857,093 US20080005956A1 (en) 2004-05-14 2007-09-18 Methods and compositions for controlling bulk density of coking coal

Related Parent Applications (2)

Application Number Title Priority Date Filing Date
US11/490,193 Continuation-In-Part US7398935B2 (en) 2004-05-14 2006-07-20 Methods and compositions for dust control and freeze control
US11/561,150 Continuation-In-Part US20080115409A1 (en) 2004-05-14 2006-11-17 Alternative fuel comprising combustible solids and by-products or waste material from industrial processes

Related Child Applications (1)

Application Number Title Priority Date Filing Date
US12/356,352 Continuation-In-Part US20090127499A1 (en) 2004-05-14 2009-01-20 Methods and compositions for dust control and freeze conditioning

Publications (1)

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US20080005956A1 true US20080005956A1 (en) 2008-01-10

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US11/857,093 Abandoned US20080005956A1 (en) 2004-05-14 2007-09-18 Methods and compositions for controlling bulk density of coking coal

Country Status (12)

Country Link
US (1) US20080005956A1 (es)
EP (2) EP2479240A1 (es)
JP (1) JP2010539298A (es)
CN (1) CN101802133B (es)
AU (1) AU2008302481B2 (es)
BR (1) BRPI0815519B1 (es)
CA (1) CA2698391C (es)
CL (1) CL2008002774A1 (es)
MX (1) MX2010002798A (es)
TW (1) TW200914602A (es)
WO (1) WO2009039070A2 (es)
ZA (1) ZA201001784B (es)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090025276A1 (en) * 2006-11-17 2009-01-29 Tran Bo L Alternative fuel comprising solids and by_products or waste material from industrial processes
US20090127499A1 (en) * 2004-05-14 2009-05-21 Tran Bo L Methods and compositions for dust control and freeze conditioning
EP2103671A1 (de) * 2008-03-20 2009-09-23 Carl Warrlich GmbH Anzünder für feste Brennstoffe
US8955685B2 (en) 2010-12-30 2015-02-17 Nalco Company Glycerides and fatty acid mixtures and methods of using same
US9796896B2 (en) 2011-12-21 2017-10-24 Joan Lynch Fertilizer and fertilizer additive compositions and methods comprising by-products from the manufacture of fatty acid alkyl esters and/or biodiesel
EP2834330B1 (en) * 2012-04-04 2018-01-31 Nalco Company Method to inhibit the air oxidation and spontaneous combustion of coal

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112322316B (zh) * 2020-10-16 2021-09-14 太原理工大学 一种供氢添加剂及其制备和应用

Citations (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2378420A (en) * 1941-06-09 1945-06-19 Koppers Co Inc Regulating the bulk density of coke-oven charges
US2885327A (en) * 1956-05-14 1959-05-05 Consolidation Coal Co Process of coking solid carbonizable material
US4164506A (en) * 1977-03-17 1979-08-14 Kao Soap Co., Ltd. Process for producing lower alcohol esters of fatty acids
US4304636A (en) * 1980-02-19 1981-12-08 Apollo Technologies, Inc. Method for improving the bulk density and throughput characteristics of coking coal
US4426409A (en) * 1982-07-02 1984-01-17 Nalco Chemical Company Cationic polymers for use in freeze protection of coals and minerals
US4450046A (en) * 1982-06-14 1984-05-22 Bethlehem Steel Corp. Method for increasing the wet bulk density of coking coals
US4886519A (en) * 1983-11-02 1989-12-12 Petroleum Fermentations N.V. Method for reducing sox emissions during the combustion of sulfur-containing combustible compositions
US5423351A (en) * 1991-05-13 1995-06-13 Westinghouse Electric Corporation Fastener for tube plug
US5423951A (en) * 1991-12-17 1995-06-13 Wienert; Fritz O. Process of continuously making coke of high density and strength
US5435813A (en) * 1992-01-08 1995-07-25 Evans; Joseph M. Wet bulk density control of fine aggregates
US6137294A (en) * 1999-01-21 2000-10-24 Usx Corporation Prediction of bulk density of particulates with a correlation based on moisture content
US20020148388A1 (en) * 2001-02-15 2002-10-17 Arr-Maz Products, L.P. Coating compositions containing methyl/ethyl esters and methods of using same
US20050000150A1 (en) * 2003-07-02 2005-01-06 The Procter & Gamble Company Method for combustion of pulverized coal with reduced emissions
US6890451B2 (en) * 2003-09-23 2005-05-10 Richard Sapienza Environmentally benign anti-icing or deicing fluids employing triglyceride processing by-products
US20050253109A1 (en) * 2004-05-14 2005-11-17 Tran Bo L Product for dust control and freeze control
US7108800B2 (en) * 2004-05-14 2006-09-19 Nalco Company Method for preventing the agglomeration or generation of dust from a particulate material comprising coal
US7126032B1 (en) * 2006-03-23 2006-10-24 Sunoco, Inc. (R&M) Purification of glycerin
US20060284137A1 (en) * 2004-05-14 2006-12-21 Tran Bo L Methods and compositions for dust control and freeze control
US20080115409A1 (en) * 2006-11-17 2008-05-22 Tran Bo L Alternative fuel comprising combustible solids and by-products or waste material from industrial processes
US20080194847A1 (en) * 2005-05-20 2008-08-14 Solvay (Societe Anonyme) Method for Preparing Chlorohydrin By Converting Polyhydroxylated Aliphatic Hydrocarbons

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
PT1227143E (pt) * 2001-01-29 2005-07-29 Cognis Deutschland Gmbh Aditivos para combustivel
KR100748158B1 (ko) 2007-05-23 2007-08-10 주식회사 신승오앤에프 글리세린과 알콜을 이용한 장입제

Patent Citations (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2378420A (en) * 1941-06-09 1945-06-19 Koppers Co Inc Regulating the bulk density of coke-oven charges
US2885327A (en) * 1956-05-14 1959-05-05 Consolidation Coal Co Process of coking solid carbonizable material
US4164506A (en) * 1977-03-17 1979-08-14 Kao Soap Co., Ltd. Process for producing lower alcohol esters of fatty acids
US4304636A (en) * 1980-02-19 1981-12-08 Apollo Technologies, Inc. Method for improving the bulk density and throughput characteristics of coking coal
US4450046A (en) * 1982-06-14 1984-05-22 Bethlehem Steel Corp. Method for increasing the wet bulk density of coking coals
US4426409A (en) * 1982-07-02 1984-01-17 Nalco Chemical Company Cationic polymers for use in freeze protection of coals and minerals
US4886519A (en) * 1983-11-02 1989-12-12 Petroleum Fermentations N.V. Method for reducing sox emissions during the combustion of sulfur-containing combustible compositions
US5423351A (en) * 1991-05-13 1995-06-13 Westinghouse Electric Corporation Fastener for tube plug
US5423951A (en) * 1991-12-17 1995-06-13 Wienert; Fritz O. Process of continuously making coke of high density and strength
US5435813A (en) * 1992-01-08 1995-07-25 Evans; Joseph M. Wet bulk density control of fine aggregates
US6137294A (en) * 1999-01-21 2000-10-24 Usx Corporation Prediction of bulk density of particulates with a correlation based on moisture content
US20020148388A1 (en) * 2001-02-15 2002-10-17 Arr-Maz Products, L.P. Coating compositions containing methyl/ethyl esters and methods of using same
US20050000150A1 (en) * 2003-07-02 2005-01-06 The Procter & Gamble Company Method for combustion of pulverized coal with reduced emissions
US7195656B2 (en) * 2003-07-02 2007-03-27 Procter & Gamble Company Method for combustion of pulverized coal with reduced emissions
US6890451B2 (en) * 2003-09-23 2005-05-10 Richard Sapienza Environmentally benign anti-icing or deicing fluids employing triglyceride processing by-products
US20050253109A1 (en) * 2004-05-14 2005-11-17 Tran Bo L Product for dust control and freeze control
US7108800B2 (en) * 2004-05-14 2006-09-19 Nalco Company Method for preventing the agglomeration or generation of dust from a particulate material comprising coal
US20060284137A1 (en) * 2004-05-14 2006-12-21 Tran Bo L Methods and compositions for dust control and freeze control
US7398935B2 (en) * 2004-05-14 2008-07-15 Nalco Company Methods and compositions for dust control and freeze control
US20080194847A1 (en) * 2005-05-20 2008-08-14 Solvay (Societe Anonyme) Method for Preparing Chlorohydrin By Converting Polyhydroxylated Aliphatic Hydrocarbons
US7126032B1 (en) * 2006-03-23 2006-10-24 Sunoco, Inc. (R&M) Purification of glycerin
US20080115409A1 (en) * 2006-11-17 2008-05-22 Tran Bo L Alternative fuel comprising combustible solids and by-products or waste material from industrial processes

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20090127499A1 (en) * 2004-05-14 2009-05-21 Tran Bo L Methods and compositions for dust control and freeze conditioning
US20090025276A1 (en) * 2006-11-17 2009-01-29 Tran Bo L Alternative fuel comprising solids and by_products or waste material from industrial processes
EP2103671A1 (de) * 2008-03-20 2009-09-23 Carl Warrlich GmbH Anzünder für feste Brennstoffe
WO2010042590A1 (en) * 2008-10-07 2010-04-15 Nalco Company Alternative fuel comprising solids and by-products or waste material from industrial processes
US8955685B2 (en) 2010-12-30 2015-02-17 Nalco Company Glycerides and fatty acid mixtures and methods of using same
US10384958B2 (en) 2010-12-30 2019-08-20 Ecolab Usa Inc. Glycerides and fatty acid mixtures and methods of using same
US9796896B2 (en) 2011-12-21 2017-10-24 Joan Lynch Fertilizer and fertilizer additive compositions and methods comprising by-products from the manufacture of fatty acid alkyl esters and/or biodiesel
EP2834330B1 (en) * 2012-04-04 2018-01-31 Nalco Company Method to inhibit the air oxidation and spontaneous combustion of coal

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