WO2016191019A2 - Coal dust treatment methods and compositions - Google Patents

Coal dust treatment methods and compositions Download PDF

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Publication number
WO2016191019A2
WO2016191019A2 PCT/US2016/029519 US2016029519W WO2016191019A2 WO 2016191019 A2 WO2016191019 A2 WO 2016191019A2 US 2016029519 W US2016029519 W US 2016029519W WO 2016191019 A2 WO2016191019 A2 WO 2016191019A2
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WO
WIPO (PCT)
Prior art keywords
oxyl
tetramethylpiperidin
coal
recited
bis
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PCT/US2016/029519
Other languages
French (fr)
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WO2016191019A3 (en
Inventor
Michael T. Raab
Seethalakshmi Suresh
Anilkumar LOKARE
Chaitra M.N.
Original Assignee
General Electric Company
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Application filed by General Electric Company filed Critical General Electric Company
Priority to CA2986900A priority Critical patent/CA2986900A1/en
Priority to KR1020177037078A priority patent/KR20180012296A/en
Priority to CN201680030579.3A priority patent/CN107835850A/en
Priority to EP16734487.8A priority patent/EP3303525A2/en
Priority to AU2016266725A priority patent/AU2016266725B2/en
Priority to US15/576,114 priority patent/US20180346834A1/en
Priority to JP2017561287A priority patent/JP2018515675A/en
Publication of WO2016191019A2 publication Critical patent/WO2016191019A2/en
Publication of WO2016191019A3 publication Critical patent/WO2016191019A3/en

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/24Combating dust during shaping or briquetting; Safety devices against explosion
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/04Raw material of mineral origin to be used; Pretreatment thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L5/00Solid fuels
    • C10L5/02Solid fuels such as briquettes consisting mainly of carbonaceous materials of mineral or non-mineral origin
    • C10L5/26After-treatment of the shaped fuels, e.g. briquettes
    • C10L5/32Coating
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L2200/00Components of fuel compositions
    • C10L2200/04Organic compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/08Inhibitors
    • C10L2230/081Anti-oxidants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L2230/00Function and purpose of a components of a fuel or the composition as a whole
    • C10L2230/14Function and purpose of a components of a fuel or the composition as a whole for improving storage or transport of the fuel
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L2250/00Structural features of fuel components or fuel compositions, either in solid, liquid or gaseous state
    • C10L2250/04Additive or component is a polymer

Definitions

  • the present invention pertains to methods for treating coal and coal piles to inhibit fugitive coal dust dissemination, and coal auto-oxidation.
  • Coal is a carbonaceous solid fossil fuel. It is extracted (mined) by surface or underground methods. Coal that is not yet mined, but is in the ground, that may or may not be exposed to the outside conditions is referred to as in-situ coal.
  • Mined coal is usually crushed to a smaller size for transportation, handling and storage.
  • the usual size for this crushed coal is less than eight inches (less than 200 mm).
  • This invention treats both in-situ coal and extracted (mined) coal during transportation, handling and storage.
  • mined coal can generate coal dust.
  • Coal dust dissemination poses safety, health and environmental concerns.
  • Coal dust suppression is desirable to minimize coal dust dissemination that may occur during coal pile storage or transit. Airborne fugitive coal dust particulates can lead to black lung disease and other illnesses.
  • Coal has traditionally been stored in piles to reduce the intrusion of air and moisture and to thereby mitigate the oxidation process. Piling does not halt coal oxidation but is merely an attempt to slow the oxidation rate.
  • the ideal coal pile is large enough to reduce the surface to volume ratio of the coal exposed to air, yet small enough that heat generated within the coal pile is dissipated into the surrounding environment.
  • the large quantity of coal utilized makes ideal conditions difficult to achieve and incidents of coal self-ignition resulting from coal oxidation are common occurrences.
  • Coal fires and coal dust explosions pose serious dangers to personnel and are costly in terms of damaged equipment and consumed coal.
  • coal may be treated with aqueous based foam in order to suppress dissemination of the fine coal dust particles, or to aid in the application of a dust control binder.
  • foams may be formed and applied as set forth, for example, in U.S. Patent 4,400,220 (Cole).
  • Foaming agents such as certain amphoteric surfactants, anionic surfactants and nonionic surfactants may be employed to aid in foam building and dust suppression. Stability of the foam is an important
  • a method of treating coal wherein a nitroxyl radical compound (NRC), an amine functionalized tannin or a quaternary ammonium compound is added to the coal.
  • NRC nitroxyl radical compound
  • the NRC is added to the coal in an amount of about 0.001 to 10 pounds per ton of coal with an addition rate of about 0.005-1 pound of the NRC per ton of coal also being noted as exemplary.
  • a foaming agent such as those selected from the group of amphoteric, nonionic and anionic surfactants can be used.
  • the NRC can be conjointly used with the surfactant to enhance foam stability and durability.
  • the foaming agents include anionic surfactants and those comprising a long chain Cii-Cis alkenyl sulfonate salt such as C11-C16 alkenyl sodium sulfonate.
  • the RC can be employed conjointly with a dust control agent (DC A) and applied to the coal.
  • the DC A may, for example, comprise a variety of different polymers.
  • the DCA comprises polymers chosen from i) epichlorohydrin (EPI)/polyalkylene polyamine/adipic acid terpolymers; ii) aminoalkylated polyacrylamides, and iii) quaternary ammonium polymers and copolymers.
  • EPI epichlorohydrin
  • polyalkylene polyamine/adipic acid terpolymers ii) aminoalkylated polyacrylamides
  • quaternary ammonium polymers and copolymers quaternary ammonium polymers and copolymers.
  • Aqueous compositions comprised of a) a nitroxyl radical (NRC) and one or more of b) dust control agent and c) foaming agent may be utilized where if a) and b) are present, for every 1-5 parts of a), there are 1-100 parts of b). If a) and c) are present, for every 1-5 parts of a) there are 0.01-10 parts of c). If all three of a) and b) and c) are present, for every 1-5 parts of a) there are 1-100 parts of b) and 0.01-10 parts of c).
  • NRC nitroxyl radical
  • a composition is comprised of the components described above where if a) and b) are present, for every 1 parts of a), there are 1-20 parts of b). If a) and c) are present, for every 1 part of a) there are 0.15- 2 parts of c). If all three of a) and b) and c) are present, for every 1 part of a) there are 1-20 parts of b) and 0.15-2 parts of c).
  • a nitroxyl radical compound is provided to treat coal surfaces, such as coal piles, to retard coal auto-oxidation, self-heating and spontaneous combustion.
  • the nitroxyl radical compound is used conjointly with a DCA such as a polymer to improve the dust control efficacy in its ability to agglomerate fine particles and inhibit dust dissemination.
  • the NRC is added to the DCA along with an anionic foaming agent.
  • the NRC and foaming agent can be added without DCA.
  • the use of NRC with the foaming agent improves foam quality and stability.
  • the NRC can have the following structure:
  • R.2, R3, R 8 , R9 are each independently of one another substituted or un-substituted Ci - Ci 8 alkyl, C2 - Ci 8 alkenyl, or C2 - Ci 8 alkynyl; or
  • R2 and R3 and/or R 8 and R9 together form with the linking carbon a C3 - C12 cycloalkyl radical
  • R 4 , R5, R 6 , R7 are each independently of one another hydrogen, substituted or un- substituted Ci - Ci 8 alkyl, C2 - Ci 8 alkenyl, or C2 - Ci 8 alkynyl;
  • Rio is hydrogen, phenyl, or substituted or unsubstituted Ci - Ci 8 alkyl
  • Ri is hydrogen, phenyl, substituted or un-substituted Ci - Ci 8 alkyl, C2 - Ci 8 alkenyl, or C2 - Ci 8 alkynyl.
  • Rio is hydrogen, phenyl, or substituted or unsubstituted Ci - C 6 alkyl
  • Ri is hydrogen, substituted or un-substituted Ci - C 6 alkyl, C2 - C 6 alkenyl, or C2 - C 6 alkynyl.
  • Exemplary nitroxyl radical compounds include derivations of dialkyl nitroxyl radicals and l-oxyl-2,2,6,6-tetraalkylpiperidine compounds such as 1- oxyl-2,2,6,6-tetramethylpiperidine, l-oxyl-2,2,6,6-tetramethylpiperidin-4-ol (4-HT), l-oxyl-2,2,6,6-tetramethylpiperidin-4-one, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl acetate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl-2-ethylhexanoate, l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl stearate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl benzoate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl benzoate,
  • a polymer dust control agent in those situations in which dust control dissemination is desired, can be used conjointly with the NRC.
  • DCA polymer dust control agent
  • These polymer dust control agents are well known and are discussed for example in U.S. Patent 5,256,444, which is incorporated by reference herein in its entirety.
  • Exemplary polymer DCAs are i) polymers having at least two of the following monomers: epichlorohydrin (epi), polyalkylene polyamine, and adipic acid; ii) polymers including aminoalkylated polyacrylamides; and iii) quaternary ammonium polymers and copolymers.
  • the DCA polymer has three of the following monomers: epichlorohydrin (epi), polyalkylene polyamine, and adipic acid; ii) polymers including aminoalkylated polyacrylamides; and iii) quaternary ammonium polymers and copolymers.
  • Exemplary members of these monomers in i) above are diethyltriamine, adipic acid and epichlorohydrin (epi), and other examples of DCAs can include ii) aminomethylated polyacrylamides, and iii) reaction products of quaternaryamine, dimethylamine, and epi.
  • molecular weights for these polymers are 100,000 to 5,000,000. In another embodiment, molecular weights for these polymers are 300,000 to 2,500,000.
  • the NRC is added in an amount of 0.002-5 lbs per ton of coal. In other embodiments, the NRC is added in an amount of 0.0035-2.5 lbs per ton of coal. In other embodiments, the NRC is added in an amount of 0.005-1.0 lbs per ton of coal.
  • the NRC can be conjointly used with known foaming agents such as nonionic, such as alkyl polyglucoside, amphoteric, such as ether amines, or anionic, such as long chain alkenyl, surfactants.
  • the foaming agent is an anionic surfactant with long alkenyl (Cii-Cis) chain.
  • anionic surfactant is a sodium olefin (C14-C16) sulfonate.
  • the aqueous based compositions has the above a) : b) : c) components therein, with the remainder of the composition including water and possibly other minor components.
  • the RC and other components can be applied to coal in-situ or that has been extracted (mined), during transportation, handing or storage, at the mine site and or any subsequent location such as terminals, docks, storage yards, coal yards, power plants or other coal utilizing facilities.
  • Aqueous sprays are often used for application to the coal.
  • the NRC is applied by itself or in combination with or without a DCA applied as a foam.
  • foaming agents such as those mentioned above are used in combination with the NRC.
  • Example 1 In order to assess the efficacy of the materials in inhibition of coal dust self-ignition, coal self-heating tests were performed. This is an accelerated test method wherein a coal sample is heated to a predetermined temperature with a known quantity and flow of air being supplied. This method accelerates natural coal oxidation and leads to the coal reaching a thermal runaway state.
  • Chemistries are prepared at two different concentrations in water, 0.5% and 2%. The chemistries are applied to the coal at a rate so that the same amount of moisture (4%) is added to all coal samples. Measurements:
  • Temperature of the coal sample is measured and logged. Time for the coal sample to reach thermal runaway (typically at 200F) is recorded. The delay in time to thermal runaway for a treated coal sample versus blank and moisture only samples are used to evaluate anti-oxidation efficacy.
  • a coal sample is weighed to 50g.
  • the desired chemistry (or moisture blank) is applied to the coal dropwise.
  • the coal is thoroughly mixed with the solution using a stainless steel spatula.
  • the sample is mixed until homogenous, and then transferred to the reaction vessel.
  • the test apparatus consists of rectangular vessel (reaction chamber) with 6 slots to place the reaction vessels and is connected to an auto temperature logger.
  • the reaction chamber has a heater and is filled with silicone oil for heating.
  • the required temperature of oil bath is set and the reaction vessels are placed in the chamber.
  • the airflow is then started.
  • the reaction chamber heating begins and starts heating the coal samples.
  • Thermocouples are placed in the oil bath to measure the set temperature of the oil bath and continuously log bath temperature in the data acquisition system.
  • Each reaction vessel is provided with two
  • thermocouples at different points and temperature data is logged continuously.
  • One blank coal sample and one moisture blank sample are included as controls along with the treated samples. Data is continuously logged until the coal has reached thermal runway.
  • EX1 l-oxyl-2,2,6,6-tetramethylpiperidin-4-ol (4HT)
  • EX2 quaternaryamine/dimethylamine/epichlorohydrin
  • EX3 tannin/monoethanolamine/formaldehyde
  • EX-1 performs at a level of inhibition comparable to known auto-oxidation inhibition polymers, which is surprising since traditional antioxidant products are polymeric, and EX-1 is a monomer.
  • Dust Monitor - Lab scale dust monitor uses white light to determine dust levels of materials dropped into the sampling chamber.
  • EX-1 namely 4HT was added to coal without any dust control agent, and in addition to a known dust control agent, namely an aqueous aminomethylated polyacrylamide (designated as "C2"). Dust control improvement is shown in following Tables 2 and 3.
  • Table 2 shows that when 4HT alone is added to coal it has a negative impact on dust generation relative to water.
  • DCA polymer dust control agent
  • Example 3 - Foam Stability - 4HT was added to a known foaming agent, "C4", an anionic surfactant, sodium olefin (Ci4-Ci 6 ) sulfonate to determine its effect on foam stability.
  • Waring Commercial Blender (Model 7011G) marked with 50 mL graduations
  • C4 anionic surfactant, sodium olefin (Ci4-Ci 6 ) sulfonate

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Abstract

Methods and compositions for treating coal are provided. A nitroxyl radical compound is added to the coal in order to inhibit coal autooxidation. Additionally, the nitroxyl radical compound can be conjointly used with conventional dust control agents, in order to suppress fugitive coal dust dissemination. In those cases in which foamed treatment is desired to treat coal dust, the nitroxyl radical compound can be conjointly used in the foamable compositions, along with a variety of foam building surfactants such as the amphoteric, nonionic and anionic surfactants.

Description

COAL DUST TREATMENT METHODS AND COMPOSITIONS
CROSS-REFERENCE TO RELATED APPLICATION
[0001] This application claims the priority benefit of Indian Provisional Patent Application No. 2615/CHE/2015 filed May 25, 2015.
FIELD OF THE INVENTION
[0002] The present invention pertains to methods for treating coal and coal piles to inhibit fugitive coal dust dissemination, and coal auto-oxidation.
Additionally, stability of foam used to apply dust control and auto-oxidation treatments is also improved.
BACKGROUND
[0003] Coal is a carbonaceous solid fossil fuel. It is extracted (mined) by surface or underground methods. Coal that is not yet mined, but is in the ground, that may or may not be exposed to the outside conditions is referred to as in-situ coal.
Mined coal is usually crushed to a smaller size for transportation, handling and storage. The usual size for this crushed coal is less than eight inches (less than 200 mm). This invention treats both in-situ coal and extracted (mined) coal during transportation, handling and storage. During transportation, handling and storage, mined coal can generate coal dust. Coal dust dissemination poses safety, health and environmental concerns. Coal dust suppression is desirable to minimize coal dust dissemination that may occur during coal pile storage or transit. Airborne fugitive coal dust particulates can lead to black lung disease and other illnesses.
[0004] Additionally, when coal is exposed to air, it slowly oxidizes to form CO2 and heat. Oxidation is accelerated in the presence of moisture and elevated temperature. Oxidation is a detrimental process since it reduces the caloric heating value of coal and can cause spontaneous combustion, or coal self-ignition. In some instances where coal self-ignition occurs in the presence of airborne coal dust, coal dust explosions can also occur.
[0005] Coal has traditionally been stored in piles to reduce the intrusion of air and moisture and to thereby mitigate the oxidation process. Piling does not halt coal oxidation but is merely an attempt to slow the oxidation rate. The ideal coal pile is large enough to reduce the surface to volume ratio of the coal exposed to air, yet small enough that heat generated within the coal pile is dissipated into the surrounding environment. Unfortunately, in large coal handling facilities, such as those existing at coal fueled power plants, the large quantity of coal utilized makes ideal conditions difficult to achieve and incidents of coal self-ignition resulting from coal oxidation are common occurrences. Coal fires and coal dust explosions pose serious dangers to personnel and are costly in terms of damaged equipment and consumed coal.
[0006] In many cases, coal may be treated with aqueous based foam in order to suppress dissemination of the fine coal dust particles, or to aid in the application of a dust control binder. These foams may be formed and applied as set forth, for example, in U.S. Patent 4,400,220 (Cole). Foaming agents such as certain amphoteric surfactants, anionic surfactants and nonionic surfactants may be employed to aid in foam building and dust suppression. Stability of the foam is an important
characteristic for maximum surface area contact with the coal surfaces during application.
[0007] Overall, in regard to coal storage and transit problems such as those noted above, a versatile product is desired to treat these problems, and desirably such a product would also enhance foam life stability in those situations in which foamed applications are utilized.
SUMMARY OF THE INVENTION
[0008] In one embodiment, a method of treating coal is provided wherein a nitroxyl radical compound (NRC), an amine functionalized tannin or a quaternary ammonium compound is added to the coal. Typically, the NRC is added to the coal in an amount of about 0.001 to 10 pounds per ton of coal with an addition rate of about 0.005-1 pound of the NRC per ton of coal also being noted as exemplary.
[0009] In some cases it is desirable to provide foamed treatments to the coal and, in this regard, a foaming agent such as those selected from the group of amphoteric, nonionic and anionic surfactants can be used. In these cases the NRC can be conjointly used with the surfactant to enhance foam stability and durability. In one embodiment, the foaming agents include anionic surfactants and those comprising a long chain Cii-Cis alkenyl sulfonate salt such as C11-C16 alkenyl sodium sulfonate. [0010] In other embodiments, the RC can be employed conjointly with a dust control agent (DC A) and applied to the coal. The DC A may, for example, comprise a variety of different polymers. In one embodiment, the DCA comprises polymers chosen from i) epichlorohydrin (EPI)/polyalkylene polyamine/adipic acid terpolymers; ii) aminoalkylated polyacrylamides, and iii) quaternary ammonium polymers and copolymers.
[0011] In most cases, the NRC will be applied to the coal in the form of an aqueous solution or dispersion. Aqueous compositions comprised of a) a nitroxyl radical (NRC) and one or more of b) dust control agent and c) foaming agent may be utilized where if a) and b) are present, for every 1-5 parts of a), there are 1-100 parts of b). If a) and c) are present, for every 1-5 parts of a) there are 0.01-10 parts of c). If all three of a) and b) and c) are present, for every 1-5 parts of a) there are 1-100 parts of b) and 0.01-10 parts of c). In another embodiment, a composition is comprised of the components described above where if a) and b) are present, for every 1 parts of a), there are 1-20 parts of b). If a) and c) are present, for every 1 part of a) there are 0.15- 2 parts of c). If all three of a) and b) and c) are present, for every 1 part of a) there are 1-20 parts of b) and 0.15-2 parts of c).
DETAILED DESCRIPTION
[0012] In one exemplary embodiment of the invention, a nitroxyl radical compound (NRC) is provided to treat coal surfaces, such as coal piles, to retard coal auto-oxidation, self-heating and spontaneous combustion. In other embodiments, the nitroxyl radical compound is used conjointly with a DCA such as a polymer to improve the dust control efficacy in its ability to agglomerate fine particles and inhibit dust dissemination.
[0013] In another aspect of the invention in which foamed application to coal is desired, the NRC is added to the DCA along with an anionic foaming agent. The NRC and foaming agent can be added without DCA. The use of NRC with the foaming agent improves foam quality and stability.
[0014] In one embodiment, the NRC can have the following structure:
Figure imgf000005_0001
where
R.2, R3, R8, R9 are each independently of one another substituted or un-substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl; or
R2 and R3 and/or R8 and R9 together form with the linking carbon a C3 - C12 cycloalkyl radical
R4, R5, R6, R7 are each independently of one another hydrogen, substituted or un- substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl;
X is -0-, -O-C(O) -, =0, - R10- or - Rio-C(O) -;
Rio is hydrogen, phenyl, or substituted or unsubstituted Ci - Ci8 alkyl
Ri is hydrogen, phenyl, substituted or un-substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl.
[0015] In another embodiment, R2, R3, R8, R9 are each independently of one another substituted or un-substituted Ci - C6 alkyl, C2 - C6 alkenyl, or C2 - C6 alkynyl; R2 and R3 and/or R8 and R9 together form with the linking carbon a C3 - C12 cycloalkyl radical; R4, R5, R6, R7 are each independently of one another hydrogen, substituted or un-substituted Ci - C6 alkyl, C2 - C6 alkenyl, or C2 - C6 alkynyl; X is -0-, -O-C(O) -, =0, - R10- or - Rio-C(O) -;
Rio is hydrogen, phenyl, or substituted or unsubstituted Ci - C6 alkyl, Ri is hydrogen, substituted or un-substituted Ci - C6 alkyl, C2 - C6 alkenyl, or C2 - C6 alkynyl. [0016] Exemplary nitroxyl radical compounds (NRC) include derivations of dialkyl nitroxyl radicals and l-oxyl-2,2,6,6-tetraalkylpiperidine compounds such as 1- oxyl-2,2,6,6-tetramethylpiperidine, l-oxyl-2,2,6,6-tetramethylpiperidin-4-ol (4-HT), l-oxyl-2,2,6,6-tetramethylpiperidin-4-one, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl acetate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl-2-ethylhexanoate, l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl stearate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl benzoate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl 4-tert-butylbenzoate, bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)succinate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4- yl)adipate, bis(l-oxyl-2,2,6,6-tetramethypiperidin-4-yl)sebacate, bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)n-butylmalonate, bis(l-oxyl-2,2,6,6-tetramethylpiperadin-4- yl)phthalate, bis(l-oxyl-2,2,6,6-tetramethylpiperidinyl-4-yl)isophthalate, bis(l-oxyl- 2,2,6,6-tetramethylpiperidinyl-4-yl)terephthalate, bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)hexahydroterephthalate, N,N'-bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)adipamide, N-l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl- dodecyl succinimide, l-oxyl-4-methoxy-2,2,6,6-tetramethylpiperidine, l-oxyl-4- amino-2,2,6,6-tetramethylpiperidine, 4-butoxy-2,2,6,6-tetramethylpiperidine and 1- oxyl-4-acetamino-2,2,6,6-tetramethylpiperidine. In one embodiment, the nitroxyl radical compound is 4HT.
[0017] In one aspect of the invention, in those situations in which dust control dissemination is desired, a polymer dust control agent (DCA) can be used conjointly with the NRC. These polymer dust control agents are well known and are discussed for example in U.S. Patent 5,256,444, which is incorporated by reference herein in its entirety. Exemplary polymer DCAs are i) polymers having at least two of the following monomers: epichlorohydrin (epi), polyalkylene polyamine, and adipic acid; ii) polymers including aminoalkylated polyacrylamides; and iii) quaternary ammonium polymers and copolymers. In another embodiment, the DCA polymer has three of the following monomers: epichlorohydrin (epi), polyalkylene polyamine, and adipic acid; ii) polymers including aminoalkylated polyacrylamides; and iii) quaternary ammonium polymers and copolymers. Exemplary members of these monomers in i) above are diethyltriamine, adipic acid and epichlorohydrin (epi), and other examples of DCAs can include ii) aminomethylated polyacrylamides, and iii) reaction products of quaternaryamine, dimethylamine, and epi. In one embodiment, molecular weights for these polymers are 100,000 to 5,000,000. In another embodiment, molecular weights for these polymers are 300,000 to 2,500,000.
[0018] Typically, from about 0.001-10 lbs of the nitroxyl radical compound is added to the coal based upon 1 ton of coal. In other embodiments, the NRC is added in an amount of 0.002-5 lbs per ton of coal. In other embodiments, the NRC is added in an amount of 0.0035-2.5 lbs per ton of coal. In other embodiments, the NRC is added in an amount of 0.005-1.0 lbs per ton of coal.
[0019] In these cases in which foamed application to coal is used, the NRC can be conjointly used with known foaming agents such as nonionic, such as alkyl polyglucoside, amphoteric, such as ether amines, or anionic, such as long chain alkenyl, surfactants. In one embodiment, the foaming agent is an anionic surfactant with long alkenyl (Cii-Cis) chain. One such anionic surfactant is a sodium olefin (C14-C16) sulfonate.
[0020] In those situations in which the NRC is conjointly used with a DCA and/or a foaming agent, the composition can include a) and one or more of b) and c). a) = NRC
b) = DCA
c) = Foaming Agent
[0021] In one embodiment, if a) and b) are present, for every 1-5 parts of a), there are 1-100 parts of b). If a) and c) are present, for every 1-5 parts of a) there are 0.01-10 parts of c). If all three of a) and b) and c) are present, for every 1-5 parts of a) there are 1-100 parts of b) and 0.01-10 parts of c).
[0022] In another embodiment, if a) and b) are present, for every 1-5 parts of a), there are 1-75 parts of b). If a) and c) are present, for every 1-5 parts of a) there are 0.075-7.5 parts of c). If all three of a) and b) and c) are present, for every 1-5 parts of a) there are 1-75 parts of b) and 0.075-7.5 parts of c).
[0023] In yet another embodiment, if a) and b) are present, for every 1-5 parts of a), there are 1-50 parts of b). If a) and c) are present, for every 1-5 parts of a) there are 0.1-5 parts of c). If all three of a) and b) and c) are present, for every 1-5 parts of a) there are 1-50 parts of b) and 0.1-5 parts of c).
[0024] In one embodiment, if a) and b) are present, for every 1 parts of a), there are 1-20 parts of b). If a) and c) are present, for every 1 part of a) there are 0.15- 2 parts of c). If all three of a) and b) and c) are present, for every 1 part of a) there are 1-20 parts of b) and 0.15-2 parts of c).
[0025] In one embodiment, the aqueous based compositions has the above a) : b) : c) components therein, with the remainder of the composition including water and possibly other minor components.
[0026] The RC and other components can be applied to coal in-situ or that has been extracted (mined), during transportation, handing or storage, at the mine site and or any subsequent location such as terminals, docks, storage yards, coal yards, power plants or other coal utilizing facilities. Aqueous sprays are often used for application to the coal. In one embodiment, the NRC is applied by itself or in combination with or without a DCA applied as a foam. For foamed applications, foaming agents such as those mentioned above are used in combination with the NRC.
EXAMPLES
Coal Auto-Oxidation Inhibition
[0027] Example 1 - In order to assess the efficacy of the materials in inhibition of coal dust self-ignition, coal self-heating tests were performed. This is an accelerated test method wherein a coal sample is heated to a predetermined temperature with a known quantity and flow of air being supplied. This method accelerates natural coal oxidation and leads to the coal reaching a thermal runaway state.
Coal Sample:
[0028] Coal crushed to -250 microns
Solutions and application:
[0029] Chemistries are prepared at two different concentrations in water, 0.5% and 2%. The chemistries are applied to the coal at a rate so that the same amount of moisture (4%) is added to all coal samples. Measurements:
[0030] Temperature of the coal sample is measured and logged. Time for the coal sample to reach thermal runaway (typically at 200F) is recorded. The delay in time to thermal runaway for a treated coal sample versus blank and moisture only samples are used to evaluate anti-oxidation efficacy.
Procedure:
[0031] A coal sample is weighed to 50g. The desired chemistry (or moisture blank) is applied to the coal dropwise. The coal is thoroughly mixed with the solution using a stainless steel spatula. The sample is mixed until homogenous, and then transferred to the reaction vessel. The test apparatus consists of rectangular vessel (reaction chamber) with 6 slots to place the reaction vessels and is connected to an auto temperature logger. The reaction chamber has a heater and is filled with silicone oil for heating. The required temperature of oil bath is set and the reaction vessels are placed in the chamber. The airflow is then started. The reaction chamber heating begins and starts heating the coal samples. Thermocouples are placed in the oil bath to measure the set temperature of the oil bath and continuously log bath temperature in the data acquisition system. Each reaction vessel is provided with two
thermocouples at different points and temperature data is logged continuously. One blank coal sample and one moisture blank sample are included as controls along with the treated samples. Data is continuously logged until the coal has reached thermal runway.
Results are shown in Table 1.
Time to Thermal Run Away
Figure imgf000009_0001
EX1 2.0 215 45
EX2 0.5 198 28
EX2 2.0 218 48
EX3 0.5 215 45
EX3 2.0 223 53
CI = comparative = aqueous polymer, diethylaminetriamine/adipic
acid/epichlorohydrin terpolymer
C2 = comparative = aqueous polymer, aminomethylated polyacrylamide EX1 = l-oxyl-2,2,6,6-tetramethylpiperidin-4-ol (4HT) EX2 = quaternaryamine/dimethylamine/epichlorohydrin EX3 = tannin/monoethanolamine/formaldehyde
[0032] The delay in time, compared to an untreated control, for onset of thermal runaway is indicative of inhibition of auto-oxidation. In this example, EX-1 performs at a level of inhibition comparable to known auto-oxidation inhibition polymers, which is surprising since traditional antioxidant products are polymeric, and EX-1 is a monomer.
[0033] Example 2 - Dust Control Improvement
Apparatus:
[0034] Dust Monitor - Lab scale dust monitor uses white light to determine dust levels of materials dropped into the sampling chamber.
Substrate:
[0035] Coal samples, mixture of size fractions to generate sufficient dust to study.
Procedure:
[0036] Prepare solutions of various concentrations of each of the products. Prepare untreated coal substrate samples with spinning riffler to ensure uniform particle size distribution for each sample. Apply products to the coal. Dry the samples at 140F for 30 minutes. Cool at room temperature for 30 minutes. Pass samples through the Dust Monitor and record dust values. The reported value is Dust Area + Max, which is the area integrated under the curve for the sample measured over 30 seconds added to the maximum dust level recorded for the sample. Lower Dust Area + Max values are indicative of superior dust control.
[0037] In these examples, EX-1, namely 4HT was added to coal without any dust control agent, and in addition to a known dust control agent, namely an aqueous aminomethylated polyacrylamide (designated as "C2"). Dust control improvement is shown in following Tables 2 and 3.
Table 2
Dust Area
Test C2 % 4HT %
+ Max
A 0.0 5.0 213.76
B 0.0 10.0 162.31
C 0.0 20.0 116.78
D 5.0 0.0 54.93
E 2.5 2.5 36.33
F (Dl water only) 0.0 0.0 116.58
[0038] Table 2 shows that when 4HT alone is added to coal it has a negative impact on dust generation relative to water. When 4HT is added as an adjuvant to C2, a known polymer dust control agent (DCA), it synergistically improves the DCA's dust reduction performance.
Table 3
Dust Area
Test C2% 4HT%
+ Max
A 2.50 0.10 36.45
B 2.50 0.25 48.05
C 2.50 0.50 36.20
D 2.50 1.00 34.10
E 2.50 1.50 33.40
F 2.50 2.00 36.00
G 2.50 2.50 40.60
H (control) 5.00 0.00 62.15 [0039] Table 3 shows that low dosages of 4HT added as an adjuvant to C2, a known polymer dust control agent (DCA), synergistically improves the DCA's dust reduction performance.
[0040] Example 3 - Foam Stability - 4HT was added to a known foaming agent, "C4", an anionic surfactant, sodium olefin (Ci4-Ci6) sulfonate to determine its effect on foam stability.
Solutions:
[0041] 200 mL solutions at ambient temperature (72°F) Apparatus:
[0042] Waring Commercial Blender (Model 7011G) marked with 50 mL graduations
Measurements:
Maximum foam height (to nearest 25 mL)
½ life time (in sec) - time for lOOmL of solution to drain back into liquid phase
Procedure:
[0043] 200mL of solution was poured into the blender. The blender was turned on low speed for 30 seconds. The blender was then allowed to sit until half of the sample (lOOmL) returned back to liquid state. The amount of time that passed until the liquid-foam interface hit the lOOmL mark was recorded as "foam ½ life time."
Results are shown in Tables 3 and 4 Table 3
Figure imgf000012_0001
0.7 5:01 6:52 6:47 4:37
0.9 5:08 7:10 7:07 5:01
1.1 5:21 6:57 7:34 5:11
Table 4
Figure imgf000013_0001
C2 = aqueous polymer, aminomethylated polyacrylamide
C4 = anionic surfactant, sodium olefin (Ci4-Ci6) sulfonate
[0044] From Table 3 it can be seen that foam stability was improved by addition of 4HT to C4, an anionic surfactant and to the combination of C4 with C2. From Table 4, it can be seen the 4HT has no significant foaming properties of its own. Surprisingly, the combination of 4HT with C4 provided a synergistic effect with regard to foam stabilization.
[0045] Additional tests were undertaken in waters of varying hardness. These tests looked at soft (40 ppm as CaCCb), medium (80 ppm Ca as CaCCb) and very hard (600 ppm Ca as CaCCb) waters. Changes in hardness can affect stable foam generation. As shown in Table 5, at all three of these hardness levels, the
combination of C4 (0.3.% or 0.5%) with 4HT (various concentrations) improved foam stability.
Table 5
Foam 1/2 Life (min:sec)
C4% 4HT % 40 ppm 80 ppm 600 ppm
0.3 0.0 3:59 4:05 2:19
0.3 0.5 4:35 4:38 3:49
0.3 1.0 5:26 5:50 5:01
0.3 1.5 5:24 6:21 5:16
0.5 0.0 4:36 4:47 3:02
0.5 0.5 5:16 5:32 4:28
0.5 1.0 6:14 6:29 5:36
0.5 1.5 6:07 6:56 5:55

Claims

1. A method of treating coal comprising adding a nitroxyl radical compound (NRC) to said coal.
2. The method of claim 1, wherein the NRC has the following structure:
Figure imgf000014_0001
wherein
R2, R3, R8, R9 are each independently of one another substituted or un-substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl; or
R2 and R3 and/or R8 and R9 together form, with the linking carbon, a C3 - C12 cycloalkyl radical; and
R4, R5, R6, R7 are each independently of one another hydrogen, substituted or un- substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl;
X is -0-, -O-C(O) -, =0, -NRio- or -NRio-C(O) -; wherein
Rio is hydrogen, phenyl, or Ci - Ci8 alkyl; and wherein
Ri is hydrogen, phenyl, substituted or un-substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl.
3. A method as recited in claim 1 wherein said NRC is added to said coal in an amount of about 0.001 to 10 lbs, per ton of coal.
4. A method as recited in claim 1 wherein said RC is selected from the group consisting of dialkyl nitroxyl radicals, l-oxyl-2,2,6,6-tetraalkylpiperidine compounds, l-oxyl-2,2,6,6-tetramethylpiperidine, l-oxyl-2,2,6,6-tetramethylpiperidin-4-ol (4-HT), l-oxyl-2,2,6,6-tetramethylpiperidin-4-one, l-oxyl-2,2,6,6-tetramethylpiperidine-4-yl acetate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl-2-ethylhexanoate, l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl stearate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl benzoate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl 4-tert-butylbenzoate, bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)succinate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4- yl)adipate, bis(l-oxyl-2,2,6,6-tetramethypiperidin-4-yl)sebacate, bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)n-butylmalonate, bis(l-oxyl-2,2,6,6-tetramethylpiperadin-4- yl)phthalate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl)isophthalate, bis(l-oxyl- 2,2,6,6-tetramethylpiperidinyl-4-yl)terephthalate, bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)hexahydroterephthalate, N,N'-bis(l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl)adipamide, N-l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl- dodecyl succinimide, l-oxyl-4-methoxy-2,2,6,6-tetramethylpiperidine, l-oxyl-4- amino-2,2,6,6-tetramethylpiperidine, 4-butoxy-2,2,6,6-tetramethylpiperidine and 1- oxyl-4-acetamino-2,2,6,6-tetramethylpiperidine and derivatives thereof.
5. A method as recited in claim 4 wherein said NRC is l-oxyl-2,2,6,6- tetramethylpiperdin-4-ol (4HT).
6. A method as recited in claim 1 wherein said method further comprises adding a foaming agent selected from amphoteric, nonionic and anionic surfactants to said coal.
7. A method as recited in claim 6 wherein said foaming agent comprises an anionic surfactant.
8. A method as recited in claim 7 wherein said anionic surfactant comprises an alkane sulfonate or an alkenyl sulfonate.
9. A method as recited in claim 1 wherein said method further comprises adding a dust control agent (DC A) to said coal.
10. A method as recited in claim 9 wherein said DCA comprises a polymer.
11. A method as recited in claim 10 wherein said polymer is a member selected from the group consisting of i) polymers containing two or more of epichlorohydrin, polyalkylene polyamine, and adipic acid monomers, ii) aminoalkylated
polyacrylamides, and iii) quaternary ammonium polymers or copolymers.
12. A method as recited in claim 1 1 wherein said i) polymers containing two or more of epichlorohydrin, polyalkylene polyamine, and adipic acid monomers comprise diethyltriamine, adipic acid, and epichlorohydrin monomers, wherein said ii) aminoalkylated polyacrylamides comprise aminomethylated polyacrylamides, and wherein the iii) quaternary ammonium polymers or copolymers comprise a reaction product of quaternaryamine, dimethylamine, and epicholohydrin.
13. A composition comprising a) a nitroxyl radical composition ( RC) and one or more of b) dust control agent and c) foaming agent, wherein if a) and b) are present, for every 1-5 parts of a), there are 1-100 parts of b), and wherein if a) and c) are present, for every 1-5 parts of a) there are 0.01-10 parts of c), and wherein if all three of a) and b) and c) are present, for every 1-5 parts of a) there are 1-100 parts of b) and 0.01-10 parts of c).
A composition as recited in claim 13, wherein the NRC has the
Figure imgf000017_0001
wherein
R2, R3, R8, R9 are each independently of one another substituted or un-substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl; or
R2 and R3 and/or R8 and R9 together form, with the linking carbon, a C3 - C12 cycloalkyl radical; and
R4, R5, R6, R7 are each independently of one another hydrogen, substituted or un- substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl;
X is -0-, -O-C(O) -, =0, -NR10- or -NRio-C(O) -; wherein
Rio is hydrogen, phenyl, or Ci - Ci8 alkyl; and wherein
Ri is hydrogen, phenyl, substituted or un-substituted Ci - Ci8 alkyl, C2 - Ci8 alkenyl, or C2 - Ci8 alkynyl.
15. A composition as recited in claim 13 wherein said a) NRC is selected from the group consisting of dialkyl nitroxyl radicals, l-oxyl-2,2,6,6-tetraalkylpiperidine compounds, l-oxyl-2,2,6,6-tetramethylpiperidine, l-oxyl-2,2,6,6- tetramethylpiperidin-4-ol (4-HT), l-oxyl-2,2,6,6-tetramethylpiperidin-4-one, 1-oxyl- 2,2,6,6-tetramethylpiperidin-4-yl acetate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl-2- ethylhexanoate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl stearate, l-oxyl-2,2,6,6- tetramethylpiperidin-4-yl benzoate, l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl 4-tert- butylbenzoate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl)succinate, bis(l-oxyl- 2,2,6,6-tetramethylpiperidin-4-yl)adipate, bis(l-oxyl-2,2,6,6-tetramethypiperidin-4- yl)sebacate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl)n-butylmalonate, bis(l-oxyl- 2,2,6,6-tetramethylpiperadin-4-yl)phthalate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin- 4-yl)isophthalate, bis(l-oxyl-2,2,6,6-tetramethylpiperidin-4-yl)terephthalate, bis(l- oxyl-2,2,6,6-tetramethylpiperidin-4-yl)hexahydroterephthalate, N,N'-bis(l-oxyl- 2,2,6,6-tetramethylpiperidin-4-yl)adipamide, N-l-oxyl-2,2,6,6-tetramethylpiperidin-4- yl-dodecyl succinimide, l-oxyl-4-methoxy-2,2,6,6-tetramethylpiperidine, l-oxyl-4- amino-2,2,6,6-tetramethylpiperidine, 4-butoxy-2,2,6,6-tetramethylpiperidine and 1- oxyl-4-acetamino-2,2,6,6-tetramethylpiperidine and derivatives thereof.
16. A composition as recited in claim 15 wherein said NRC is l-oxyl-2,2,6,6- tetramethypiperdin-4-ol (4HT).
17. A composition as recited in claim 13, wherein the foaming agent is selected from amphoteric, nonionic and anionic surfactants.
18. A composition as recited in claim 17, wherein the foaming agent comprises an anionic surfactant.
19. A composition as recited in claim 18, wherein the anionic surfactant comprises an alkane sulfonate or an alkenyl sulfonate.
20. A composition as recited in claim 13, wherein said dust control agent comprises a polymer.
21. A composition as recited in claim 20, wherein said polymer is a member selected from the group consisting of i) polymers containing two or more of epichlorohydrin, polyalkylene polyamine, and adipic acid monomers, ii)
aminoalkylated polyacrylamides, and iii) quaternary ammonium polymers or copolymers.
22. A composition as recited in claim 21, wherein said i) polymers containing two or more of epichlorohydrin, polyalkylene polyamine, and adipic acid monomers comprise diethyltriamine, adipic acid, and epichlorohydrin monomers, wherein said ii) aminoalkylated polyacrylamides comprise aminomethylated polyacrylamides, and wherein the iii) quaternary ammonium polymers or copolymers comprise a reaction product of quaternaryamine, dimethylamine, and epicholohydrin.
23. A composition comprising coal and a) a nitroxyl radical composition ( RC) and one or more of b) dust control agent and c) foaming agent, wherein if a) and b) are present, for every 1-5 parts of a), there are 1-100 parts of b), and wherein if a) and c) are present, for every 1-5 parts of a) there are 0.01-10 parts of c), and wherein if all three of a) and b) and c) are present, for every 1-5 parts of a) there are 1-100 parts of b) and 0.01-10 parts of c), and wherein a) is present in an amount of about 0.001 to 10 lbs per ton of the coal.
24. A method of treating coal comprising adding a quaternary ammonium compound to said coal.
25. The method of claim 24 wherein the quaternary ammonium compound is quaternary amine/dimethylamine/epichlorohydrin.
26. A method of treating coal comprising adding an amine functionalized tannin to said coal.
27. The method of claim 26, wherein the amine functionalized tannin is tannin/monoethanolamine/formaldehyde.
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