JP2006328413A - Method for producing spill-prevention agent for granular sediment - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a method for producing a spill-prevention agent having excellent performance to prevent the sliding and spill-over of granular sediment by rainfall, etc., prevent the increase of water content in the granular sediment and prevent the scattering of the sediment in a dried state. <P>SOLUTION: The agent for preventing the spill-over of granular sediment is produced by charging a mixing tank with at least an ethylene-vinyl acetate copolymer emulsion, an anionic moistening penetrant, a polyvinyl alcohol, a water-repelling agent and water and mixing the components. The addition amount of the polyvinyl alcohol is 0.05-0.7 wt.% and that of the anionic moistening penetrant is 0.005-0.05 wt.% based on the spill-prevention agent. The agent has a surface tension of 28-45 Dyne/cm and a film produced by drying the agent has a water dissolution ratio of ≤15 wt.%. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to a method for producing a spill preventive agent for granular deposits, and forms a strong bonding layer on the granular deposits to improve water resistance and the like, and prevents collapse and spillage of the granular deposits due to rainfall and the like. The present invention also relates to a method for producing an anti-spill agent that is excellent in preventing increase in water content in granular deposits and preventing scattering during drying.

  In general, granular deposits such as coal are conveyed by a conveyor and stored in a pile in an outdoor storage yard by a stacker or the like. These dry sediments are scattered by the wind during drying to generate dust, and rainwater penetrates due to rain, etc., and the water content rises, causing the water to collapse and causing problems such as energy loss due to increased water content. Arise.

  In order to prevent this collapse and outflow of the granular deposit, the surface of the granular deposit is hardened by spraying the deposit as a coating agent such as an emulsion of vinyl acetate resin, acrylic resin, or rubber latex. Method (Patent Document 1), Method of spraying a finely pulverized cement aqueous solution and then spraying an aqueous resin solution of vinyl acetate resin, acrylic resin, polyethylene, saturated polyester, etc. to solidify the surface of the granular deposit (Patent Document 2) , A method of forming a consolidated layer (a layer in which a coating agent has consolidated deposited particles) by spraying a coating agent comprising an aqueous polyvinyl alcohol solution and a curing agent and drying, a resin solution containing white powder To form a coating film by spraying (Patent Document 4), a method to spray a surface treatment agent consisting of a resin and a colorant (patent text) 5), ethylene - a method of spraying a liquid composition as main agent vinyl acetate copolymer emulsion (Patent Document 6) have been proposed.

However, the conventional method has problems such as insufficient formation of the bonding layer, an insufficient effect of suppressing the penetration of rainwater in the formed bonding layer, and time-consuming work. In particular, spill prevention agents using ethylene-vinyl acetate copolymer emulsions bind well with granular deposits on the surface due to the excellent water resistance and adhesiveness of ethylene-vinyl acetate copolymers, and penetrate rainwater. Although the suppression effect is relatively excellent, the effect is not sufficient in the case of heavy rainfall such as the rainy season, and improvement has been demanded.
JP 49-31589 A JP 58-45285 A JP-A-61-236866 JP-A-3-157492 JP-A-3-138208 Japanese Patent Laid-Open No. 48-40209

  The present invention was made in order to improve such disadvantages of the prior art, and on the granular deposit, a bonded layer composed of the granular material of the granular deposit and an outflow preventive agent is formed, Providing a method for producing a particulate sediment spillage prevention agent that has an excellent effect on preventing collapse and spillage of particulate sediment due to rainfall, preventing an increase in water content in the particulate sediment, and preventing scattering during drying. To do.

  That is, the present invention is a particulate deposit characterized by adding at least an ethylene-vinyl acetate copolymer emulsion, an anionic wet penetrant, polyvinyl alcohol, a water repellent and water to a mixing tank and mixing them. It is a manufacturing method of the outflow prevention agent.

It is preferable that the addition amount of the anionic wet penetrant is 0.005 wt% to 0.05 wt% with respect to the outflow preventive agent.
The anionic wetting penetrant is preferably composed of one or more selected from alkyl sulfosuccinate, alkyl naphthalene sulfonate, and alkyl benzene sulfonate.

It is preferable that the addition amount of the polyvinyl alcohol is 0.05 wt% to 0.7 wt% with respect to the outflow preventing agent.
It is preferable that the surface tension of the anti-spilling agent is 28 to 45 Dyne / cm, and the water elution rate of the film obtained by drying the anti-spilling agent is 15% by weight or less.

  It is preferred that the granular deposit is a deposit of coal or iron ore.

  The spillage prevention agent for the granular deposit produced by the method of the present invention is an aqueous system using an EVA emulsion, and therefore has little adverse effect on the environment. Compared to conventional synthetic resin emulsion systems, it forms a strong tie layer with granular deposits and has excellent water resistance, so collapse of granular deposits caused by water such as rain, prevention of outflow, and granular deposition It has an excellent effect in preventing an increase in the moisture content in the product.

Hereinafter, the present invention will be described in detail.
The surface tension of the spillage prevention agent (hereinafter simply referred to as “spillage prevention agent”) of the granular deposit produced by the method of the present invention is 28 to 45 Dyne / cm, preferably 30 to 45 Dyne / cm. If the surface tension is high, the effect of permeability of the spill preventive agent to the granular deposit will be low. Conversely, if the surface tension is low, there will be no problem in terms of permeability to the granular deposit. In particular, water repellency decreases. When the permeability is lowered, the outflow preventive agent does not penetrate into the granular deposit, and a thin film mainly containing the outflow preventive agent is formed on the surface of the granular deposit. On the other hand, when it has moderate permeability, the spill preventive agent penetrates into the granular deposit and forms a strong film consisting of the granular deposit and the spill preventive agent on the surface of the granular deposit. Prevents water penetration and prevents the surface from collapsing. On the other hand, if the surface tension is too low, the spill preventive agent will excessively permeate into the granular deposit and a strong film cannot be formed. In addition, such a film has reduced water resistance.

  The elution rate by water immersion of the film obtained by drying is 15% by weight or less, more preferably 10% by weight or less. If the elution rate is low, the components in the film will not flow even in heavy rain, etc., and the strength of the film will not decrease so much that the granular deposit will collapse and flow out, and the moisture content of the granular deposit will increase. The increase can be further prevented.

  An ethylene-vinyl acetate copolymer emulsion is used for the production of the anti-spill agent. The ethylene-vinyl acetate copolymer emulsion (hereinafter referred to as “EVA emulsion”) is effective in forming a bonding layer due to its excellent adhesion to a granular deposit and film formability, and the formed bonding layer. Is resistant to rainwater and has the effect of suppressing the penetration of rainwater into granular deposits.

  Although commercially available EVA emulsions can be used, those having an ethylene-vinyl acetate copolymer composition in the EVA emulsion in a weight ratio of ethylene: vinyl acetate = 5: 95 to 40:60 are particularly preferably used. . Further, as the third monomer, monocarboxylic acids such as acrylic acid and methacrylic acid and esters thereof, dicarboxylic acids such as maleic acid and itaconic acid, anhydrides, esters, vinyl esters other than vinyl acetate, and halogenated vinyls such as vinyl chloride A copolymer obtained by copolymerizing a copolymerizable monomer such as an aromatic vinyl such as styrene, a polyfunctional monomer such as triallyl cyanurate, or an amide such as acrylamide can also be used.

  An EVA emulsion using polyvinyl alcohol (hereinafter referred to as “PVA”) as an emulsifying dispersant used for polymerization is more preferably used from the viewpoints of binding properties to a granular deposit and film toughness.

  In the production method of the present invention, PVA is used as the water-soluble polymer. There is no restriction | limiting in particular as PVA to be used, and what is marketed can be used. For example, PVA obtained by saponifying a homopolymer or copolymer obtained by polymerizing one or more fatty acid vinyl esters, or a copolymer with other copolymerizable monomers, or the like The modified PVA which modified | denatured these PVA is mentioned. In the PVA, examples of other copolymerizable monomers include olefins such as ethylene and propylene: polymerizable monocarboxylic acids such as acrylic acid, methacrylic acid, and crotonic acid: polymerizable such as maleic acid and itaconic acid. Dicarboxylic acids: polymerizable dicarboxylic anhydrides such as maleic anhydride: esters of polymerizable monocarboxylic acids and polymerizable dicarboxylic acids, salts: polymerizable acid amides such as acrylamide and methacrylamide: methyl acrylate, ethyl acrylate Acrylic acid esters such as: methacrylates such as methyl methacrylate and ethyl methacrylate: monomers having a glycidyl group such as allyl glycidyl ether and glycidyl methacrylate: alkyl vinyl ethers.

  The saponification degree of PVA is preferably 65 to 100 mol%. If it is less than 65 mol%, the hydrophilicity of PVA is low, so that a liquid composition is obtained, the solubility is lowered, and a good film may not be obtained.

  The polymerization degree of PVA is preferably 100 to 4500. If it is less than 100, the film strength obtained is small and the water resistance is also poor. On the other hand, when it exceeds 4500, it becomes a high-viscosity liquid.

  Non-ionic and anionic surfactants such as water-soluble polymers other than PVA such as methyl cellulose and hydroxyethyl cellulose, polyoxyethylene alkyl ethers and salts thereof, and polyoxyethylene-polyoxypropylene block polymers also inhibit the effects of PVA. Can be used to the extent that it does not.

  PVA is preferably used in the range of 0.05% to 0.7% by weight, more preferably in the range of 0.05% to 0.4% by weight. Further, within the above range, in order to further suppress the coating strength and elution of components from the coating in the wet state with water, and to balance the strength in the wet state, 100 parts by weight of the ethylene-vinyl acetate copolymer is used for PVA. Is preferably 15 parts by weight or less. If the amount of PVA is too large, the water resistance is remarkably lowered, and if it is less than this, a granular layer and a consolidated layer having sufficient strength cannot be formed. On the other hand, if the amount is too small, it is insufficient to prevent the settling of the spill preventive agent. PVA promotes the formation of a strong tie layer consisting of the granular material of the granular deposit and the spill preventive agent. At the same time, PVA itself is water-soluble. There is a risk of being washed away. Accordingly, if too much PVA is formed to form a strong bonding layer in the dry state, the water resistance is deteriorated.

  As the anionic wetting and penetrating agent, one consisting of one or more selected from alkyl sulfosuccinate, alkyl naphthalene sulfonate, and alkyl benzene sulfonate is used. An anionic wet penetrant has a strong penetrating effect on granular deposits, lowers the surface tension of the spill preventive agent, improves wettability with the granular deposit, and reduces the spill preventive agent to a granular deposit. Improves permeability. As a result, it is possible to increase the thickness of the binding layer (film) of the spillage prevention agent and the granular deposit, which plays an important role in forming the binding layer. If the anionic wetting penetrant is not added, the spill preventive agent does not sufficiently penetrate into the granular deposit and stops at the surface or near the surface, so that it becomes only a thin film and lacks durability.

  As the alkylsulfosuccinate, sodium dialkylsulfosuccinate is preferable. As the alkyl naphthalene sulfonate, sodium alkyl naphthalene sulfonate is preferable. As the alkyl benzene sulfonate, sodium alkyl benzene sulfonate is preferable.

Among the anionic wetting penetrants, alkylsulfosuccinates are preferable, and sodium dialkylsulfosuccinate is particularly preferable.
The anionic wetting penetrant is added so that the surface tension of the spill preventive agent is 28 to 45 Dyne / cm. The amount of addition varies depending on the type of anionic wetting and penetrating agent, but is usually 0.005 wt% to 0.05 wt% in the outflow preventing agent. If the addition amount is small, there is no effect of permeability of the spill preventive agent to the granular deposit, and if it is too much, there is no problem in terms of permeability, but the water resistance of the film, particularly water repellency is lowered.

  The non-volatile content of the spill preventive agent is preferably 3% by weight to 20% by weight, and more preferably 5% by weight to 15% by weight. However, the non-volatile content of the outflow preventing agent is not limited to this. Even if the non-volatile content is low, it can be adjusted by increasing the spraying amount, and when it is high, it can be adjusted by decreasing the spraying amount. However, if the non-volatile content is too low, the resistance of the consolidated layer and the suppression of rainwater permeation tend to decrease. If the non-volatile content is high, the viscosity increases, the permeability to the granular deposit decreases, and spraying becomes difficult. When the non-volatile content is low, if the spill preventive agent is not sprayed immediately after adjustment, the resin content may settle and separate. In this case, PVA may be added to prevent sedimentation.

  The addition amount of the EVA emulsion is adjusted according to the non-volatile content of the spill preventive agent. The addition amount is preferably 3% by weight to 20% by weight, more preferably 5% by weight to 15% by weight as a nonvolatile content.

  In order to impart water repellency against rainfall or the like, a water repellent can be used in the spill preventive agent of the present invention. As the water repellent, not only a water repellent effect but also a substance that does not phase separate from other components is preferable. For example, waxes are preferable. Examples of the wax include paraffin wax, polyethylene wax, microcrystalline wax, carbana wax, and higher fatty acid ester. Among them, emulsified paraffin wax emulsion is preferable.

  The amount of water repellent used varies depending on the type, but it is the amount necessary to give water-repellent properties to the granular deposits. 2% by weight or less is preferable.

  In the spill preventive agent of the present invention, an emulsion obtained by emulsifying alumina cement, coal tar or asphalt tar with a commercially available emulsifier may be used in combination as necessary for the purpose of suppressing the penetration of rainwater into the granular sediment. I can do it. Moreover, an antifoamer, a color pigment, etc. can also be added suitably.

  In order to produce the outflow prevention agent, it can be obtained by mixing the raw material EVA emulsion and other raw materials in a mixing tank equipped with a stirrer. In this case, for example, a water-soluble polymer such as PVA which is difficult to dissolve can be mixed in a short time when added in the form of an aqueous solution. The amount of water can be appropriately adjusted including the amount of water so as to have a predetermined nonvolatile content. Alternatively, it is also possible to prepare a spill preventive stock solution that is higher than a predetermined non-volatile content, dilute it with water before use, and use it as a predetermined non-volatile spill preventive agent. In this case, the amount can be reduced when transporting the spill preventive agent. Further, when the nonvolatile content is high, it is possible to prevent the EVA emulsion from being separated and settled, which is advantageous for storage. The concentration of the non-volatile content of the stock solution for preventing spillage may be adjusted, for example, to be in the range of 20 to 70% by weight, and more preferably in the range of 25 to 60% by weight.

  The granular deposits to be sprayed with the spill preventive agent of the present invention are not particularly limited as long as they are granular deposits. For example, coal and iron ore deposits, particularly field coal deposits and field iron ores. These include granular deposits such as stone deposits, coke and iron ore, road slopes, and granular waste deposits. When the spill preventive agent of the present invention is used for these granular deposits, dust is prevented, and it is effective for preventing collapse due to rain, preventing spillage, and preventing the moisture content in the granular deposits from increasing.

About 20 to 500 g of the spill preventive agent is preferably sprayed on the granular deposit as a non-volatile component (referring to the remaining composition excluding moisture) per 1 m ^{2 of} the deposit. However, this amount does not mean that the effect is lost when spraying less or more than this, and can be appropriately changed depending on the kind of deposit, environment of spraying, and the like. The spraying can be performed uniformly over the entire surface of the sediment using a watering wheel or the like. Spraying may be performed only once, but may be performed twice or more. Moreover, even when the granular deposit is wet, it can be sprayed. A relatively uniform film can be obtained when the non-volatile content is relatively low when the granular deposit is dry, and conversely when the moisture content is high, the non-volatile content is increased.

Hereinafter, the present invention will be specifically described with reference to Examples and Comparative Examples.
Example 1
12.5 parts by weight of EVA emulsion (Denka EVA # 81 manufactured by Denki Kagaku Kogyo Co., Ltd., nonvolatile content 56% by weight) (7 parts by weight as an ethylene-vinyl acetate copolymer resin) in a mixing tank equipped with a stirrer, concentration 5% % PVA (B-33 manufactured by Denki Kagaku Kogyo Co., Ltd., saponification degree 88 mol%, polymerization degree 3300) 2 parts by weight of aqueous solution (0.1 part by weight as PVA), anionic wetting penetrant (sodium alkylsulfosuccinate) 0.018 parts by weight (0.018 parts by weight as a pure component), 0.11 parts by weight (0.03 parts by weight as a pure component), water repellent (Digit S-8 manufactured by Kyoyo Chemical Co., Ltd., nonvolatile content 28%) ) And water were added to make the whole 100 parts by weight, and the non-volatile content was 7.2% by weight. The following evaluation was performed about the obtained anti-spill agent. The results are shown in Table 1.

(Measurement of surface tension)
The anti-flow agent was measured with a Wilhelmy surface tension meter (manufactured by Kyowa Interface Science Co., Ltd.) in an atmosphere at 23 ° C.

(Measurement of water elution rate)
The spill inhibitor is dried in a thermostatic chamber at 23 ° C. for 1 week to obtain a dry film. After measuring the weight (W ₁ ) of the film, it was immersed in water for 48 hours in the same room, taken out and dried at 60 ° C. for 24 hours (W ₂ ), and the ratio of the weight loss from the weight before immersion in water was eluted with water. Rate (see the following formula (1)).

(Surface strength of granular deposits, water repellency test)
Vertical, horizontal, depth filled with coal formwork 30,30,5Cm, the inhibitor out fluid on the coal surface as 1.3 l / m ² (1m ² per nonvolatile content at atomizer 93. 6g) Sprayed and dried in a constant temperature room at 20 ° C. for 1 day. The strength of the coal surface at the end of the mold was measured with a spring-type tension gauge (a cylindrical shape with a 6φ tip at the measurement portion made by A & D Co., Ltd.) to obtain the surface strength before watering. Next, the measurement site and the boundary between the mold and the coal were sealed with a commercially available sealing agent, and again left in a constant temperature room at 20 ° C. One day later, the weight of each mold was measured, and the mold was tilted at 35 °, and 9 liters of water was sprayed at a rate of 1 liter / minute with a watering can. Immediately after the water adhering to the mold was wiped off and the weight was measured, the strength of the coal surface was measured with a spring tension gauge. The water absorption was determined from the difference in weight before and after watering, and the indicated value of the spring tension gauge was used as the surface strength after watering.

Examples 2-7 and Reference Example 1
The test was conducted in the same manner as in Example 1 except that the blending amount of the spill preventive agent used in Example 1 was changed as shown in Table 1. The test results are shown in Table 1. When the spill preventive agent of Reference Example 1 was allowed to stand for a while, the resin content settled and separated, but when the mixture was stirred and mixed again and tested, no decrease in physical properties was observed.

Comparative Example 1
A test was conducted in the same manner as in Example 1 except that the PVA used in Example 1 was increased, and the test results are shown in Table 2.

Comparative Examples 2-3
A test was conducted in the same manner as in Example 1 except that the blending amount of the spill preventive agent used in Example 1 was changed as shown in Table 2, and the test results are shown in Table 2.

  The present invention forms a strong bonded layer with the granular deposit and is excellent in water resistance, so that the granular deposit collapses due to water such as rain, prevents outflow, and the water content in the granular deposit It can be used in a method for producing a spill preventive agent for granular deposits, which is excellent in preventing the increase of slag.

Claims (6)

Production of powder sediment deposit prevention agent characterized by adding at least ethylene-vinyl acetate copolymer emulsion, anionic wet penetrant, polyvinyl alcohol, water repellent and water to a mixing tank and mixing them. Method. The method for producing a spill preventive agent for granular deposits according to claim 1, wherein the addition amount of the anionic wet penetrant is 0.005 wt% to 0.05 wt% with respect to the spill preventive agent. The outflow prevention of particulate deposits according to claim 1 or 2, wherein the anionic wet penetrant is composed of one or more selected from alkyl sulfosuccinate, alkyl naphthalene sulfonate, and alkyl benzene sulfonate. Manufacturing method. The method for producing a spill preventive agent for granular deposits according to claim 1, wherein the amount of the polyvinyl alcohol added is 0.05 wt% to 0.7 wt% with respect to the spill preventive agent. The surface tension of the outflow preventive agent is 28 to 45 Dyne / cm, and the water elution rate of a film obtained by drying the outflow preventive agent is 15% by weight or less. The manufacturing method of the outflow prevention agent of the granular deposit of description. The method for producing a spill preventive agent for a granular deposit according to any one of claims 1 to 5, wherein the granular deposit is a deposit of coal or iron ore.