JP2012077312A - Dust treatment agent composition - Google Patents

Dust treatment agent composition Download PDF

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JP2012077312A
JP2012077312A JP2012002877A JP2012002877A JP2012077312A JP 2012077312 A JP2012077312 A JP 2012077312A JP 2012002877 A JP2012002877 A JP 2012002877A JP 2012002877 A JP2012002877 A JP 2012002877A JP 2012077312 A JP2012077312 A JP 2012077312A
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dust
agent composition
polytetrafluoroethylene
aqueous dispersion
fluorine
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Kazuo Konabe
一雄 小鍋
Mitsuyoshi Kawazoe
光義 川副
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Chemours Mitsui Fluoroproducts Co Ltd
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Du Pont Mitsui Fluorochemicals Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a composition for a dust preventive treatment agent made of a fluorine-containing polymer aqueous dispersion which has high dust preventive effect equally to the conventional dust preventive composition, and which also has the low risk of an environmental problem.SOLUTION: The composition for a dust preventive treatment agent is made of a fluorine-containing polymer aqueous dispersion as an aqueous dispersion of polytetrafluoroethylene having a fluorine-containing emulsifier content of ≤50 ppm, in which the specific gravity of the polytetrafluoroethylene is ≤2.27, while the average particle diameter is 0.1 to 0.5 μm, and which contains a hydrocarbon based anionic surfactant as an emulsion stabilizer. The composition is mixed with a dusting substance, and the mixture is subjected to a compressing-shearing action at a temperature of about 20 to 200°C to fibrillate the polytetrafluoroethylene, thus is used for inhibiting the dust of the dusting substance.

Description

本発明は、防塵効果が高く、環境への懸念が少ないポリテトラフルオロエチレン(以下
PTFEという)の水性分散液からなる、発塵性物質の塵埃抑制処理剤組成物に関する。さらに詳しくは、本発明は含フッ素乳化剤が特定の低いレベルで含有されているPTFEの水性分散液からなる、防塵効果が高く、環境への懸念が少ない発塵性物質の塵埃抑制処理剤組成物に関する。
The present invention relates to a dust control agent composition for dusting substances, which is made of an aqueous dispersion of polytetrafluoroethylene (hereinafter referred to as PTFE) having a high dustproof effect and less concern for the environment. More specifically, the present invention is a dust-controlling agent composition of a dusting substance having a high dustproof effect and less environmental concerns, comprising an aqueous dispersion of PTFE containing a fluorine-containing emulsifier at a specific low level. About.

塵埃を出す粉末状物質の塵埃を抑制する技術は、健康上、安全上、環境上その他の要請から、生活のためにまた産業のために重要な技術である。
このような塵埃抑制技術としては、特公昭52−32877号公報において、PTFEを粉末状物質と混合し、該混合物に約20〜200℃の温度で圧縮−せん断作用を施すことによりPTFEをフィブリル化して粉末状物質の塵埃発生を抑制する方法が提案されている。
Technology for suppressing dust from powdery substances that generate dust is an important technology for daily life and for industry because of other health, safety, environmental and other requirements.
As such dust control technology, in Japanese Patent Publication No. 52-32877, PTFE is fibrillated by mixing PTFE with a powdery substance and subjecting the mixture to a compression-shearing action at a temperature of about 20 to 200 ° C. Thus, a method for suppressing dust generation of a powdery substance has been proposed.

PTFEは、組成としてはテトラフルオロエチレンのホモポリマーで形態としてはファインパウダー又はエマルジョンであるテフロン(登録商標)6又はテフロン(登録商標)30、並びに組成としてはテトラフルオロエチレンの変性ポリマーで形態としては同じくファインンパウダーであるテフロン(登録商標)6Cなどである。   PTFE is a homopolymer of tetrafluoroethylene in composition and fine powder or emulsion in form Teflon (registered trademark) 6 or Teflon (registered trademark) 30, and a composition in modified polymer of tetrafluoroethylene in form. It is also Teflon (registered trademark) 6C, which is also finen powder.

また、特開平8−20767号公報では、PTFEに対して1.0重量%以上の炭化水素系アニオン界面活性剤を含有する水性エマルジョンを使用する安定性のよい塵埃抑制方法が提案されており、セメントについて塵埃抑制効果があることが示されている。同公報によれば、PTFE粒子は、米国特許第2,559,752号に開示されている乳化重合法、即ちテトラフルオロエチレンを水溶性重合開始剤及びフルオロアルキル基を疎水基とするアニオン系界面活性剤(以下、含フッ素乳化剤という)を乳化剤として含む水性媒体中に圧入、重合させることにより、水性エマルジョンの形態で製造されるが、安定性を増すためにさらに乳化安定剤が添加されている。   JP-A-8-20767 proposes a stable dust control method using an aqueous emulsion containing 1.0% by weight or more of a hydrocarbon-based anionic surfactant with respect to PTFE. Cement has been shown to have a dust control effect. According to the publication, PTFE particles are produced by emulsion polymerization disclosed in US Pat. No. 2,559,752, that is, an anionic interface having tetrafluoroethylene as a water-soluble polymerization initiator and a fluoroalkyl group as a hydrophobic group. It is manufactured in the form of an aqueous emulsion by press-fitting into an aqueous medium containing an activator (hereinafter referred to as a fluorine-containing emulsifier) as an emulsifier, and polymerized, but an emulsion stabilizer is further added to increase the stability. .

最近、これらの塵埃抑制処理剤が肥料、土質安定剤、土壌改良剤、更には石炭灰などの埋立材料に大量に使用され、塵埃抑制処理剤の適用範囲が拡大したことによって、環境への影響が懸念されるようになってきた。
PTFE水性分散液に乳化剤として含まれる界面活性剤(含フッ素乳化剤)は、重合に使用されるものではあるが難分解性で環境への影響が懸念される。また生分解性ではなく環境汚染物質と分類されるため、地下水、湖沼、河川などを汚染する可能性が生じてきた。
そこで本発明者らは、塵埃抑制効果があって、環境への影響を懸念することなく塵埃を抑制できる方法の開発に鋭意注力した結果、本発明に到達したものである。
Recently, these dust control agents have been used in large amounts in fertilizers, soil stabilizers, soil conditioners, and landfill materials such as coal ash, and the scope of application of dust control agents has increased. Has become a concern.
A surfactant (fluorine-containing emulsifier) contained as an emulsifier in an aqueous PTFE dispersion is used for polymerization, but it is hardly decomposable and there is a concern about influence on the environment. Moreover, since it is not biodegradable but classified as an environmental pollutant, it has been possible to pollute groundwater, lakes and rivers.
Therefore, the present inventors have reached the present invention as a result of intensive efforts to develop a method that has a dust suppressing effect and can suppress dust without concern about the influence on the environment.

特公昭52−32877号公報Japanese Patent Publication No. 52-32877 特開平8−20767号公報JP-A-8-20767 米国特許第2,559,752号公報US Pat. No. 2,559,752

本発明者らは、PTFE水性分散液に乳化剤として含まれる界面活性剤(含フッ素乳化剤)は、PTFE水性分散液を得る重合においては不可欠のものではあるが、難分解性で環境への影響が懸念されることに着目して、環境問題の可能性が低い塵埃抑制処理剤の開発を進めた。
すなわち、本発明は、従来の塵埃抑制処理剤組成物と同等に塵埃抑制効果が高く、且つ環境問題の可能性が低い、含フッ素重合体水性分散液からなる塵埃抑制処理剤を提供することを目的とする。
The present inventors have disclosed that surfactants (fluorine-containing emulsifiers) contained as an emulsifier in PTFE aqueous dispersions are indispensable in polymerization to obtain PTFE aqueous dispersions, but are hardly decomposable and have an impact on the environment. Focusing on the concerns, we proceeded with the development of dust control agents that are less likely to cause environmental problems.
That is, the present invention provides a dust suppression treatment agent comprising a fluoropolymer aqueous dispersion having a dust suppression effect as high as that of a conventional dust suppression treatment composition and a low possibility of environmental problems. Objective.

本発明により、含フッ素乳化剤の含有率が50ppm以下であるポリテトラフルオロエチレンの水性分散液であって、該ポリテトラフルオロエチレンの比重が2.27以下であって、平均粒径が0.1〜0.5μmであり、乳化安定剤として炭化水素系アニオン系界面活性剤を含有する含フッ素重合体水性分散液からなり、発塵性物質と混合して、該混合物に約20〜200℃の温度で圧縮−剪断作用を施すことにより、ポリテトラフルオロエチレンをフィブリル化して発塵性物質の塵埃を抑制するために使用する塵埃抑制処理剤組成物が提供される。 According to the present invention, an aqueous dispersion of polytetrafluoroethylene having a fluorine-containing emulsifier content of 50 ppm or less, wherein the polytetrafluoroethylene has a specific gravity of 2.27 or less and an average particle size of 0.1 ~0.5μm der is, consists fluoropolymer aqueous dispersion contains a hydrocarbon-based anionic surfactant as an emulsion stabilizer, is mixed with dusting material, about 20 to 200 ° C. to the mixture By applying a compression-shearing action at a temperature of 1, a dust suppressing treatment agent composition used for fibrillating polytetrafluoroethylene to suppress dust of dusting substances is provided.

前記含フッ素乳化剤の含有率が50ppm以下である含フッ素重合体水性分散液が、含フッ素乳化剤を用いてテトラフルオロエチレンを重合して得られた重合体水性分散液から、含フッ素乳化剤を除去して得られたものである、前記した塵埃抑制処理剤組成物は本発明の好ましい態様である。   The fluorine-containing polymer aqueous dispersion having a content of the fluorine-containing emulsifier of 50 ppm or less is obtained by removing the fluorine-containing emulsifier from the polymer aqueous dispersion obtained by polymerizing tetrafluoroethylene using the fluorine-containing emulsifier. The above-described dust suppression treatment agent composition obtained by the above method is a preferred embodiment of the present invention.

本発明により、従来の塵埃抑制処理剤組成物と同等に塵埃抑制効果が高く、且つ環境問題の可能性が低い含フッ素重合体水性分散液からなる塵埃抑制処理剤が提供される。
本発明によれば、塵埃抑制効果が高く、且つ環境問題の可能性が低いだけでなく、高価な含フッ素乳化剤を回収し再利用することによって有効に活用することを可能とする塵埃抑制処理剤が提供される。
According to the present invention, there is provided a dust suppression treatment agent comprising a fluoropolymer aqueous dispersion having a dust suppression effect as high as that of a conventional dust suppression treatment composition and having a low possibility of environmental problems.
ADVANTAGE OF THE INVENTION According to this invention, the dust suppression processing agent which not only has a high dust suppression effect and has a low possibility of an environmental problem, but can be utilized effectively by collect | recovering and reusing an expensive fluorine-containing emulsifier. Is provided.

本発明は、含フッ素乳化剤の含有率が50ppm以下である含フッ素重合体水性分散液からなる塵埃抑制処理剤組成物を提供する。   The present invention provides a dust suppressing treatment agent composition comprising a fluoropolymer aqueous dispersion having a fluorine-containing emulsifier content of 50 ppm or less.

本発明の含フッ素重合体としては、ホモポリマーと呼ばれるテトラフルオロエチレン(TFE)の単独重合体(PTFE)と、変性ポリマーと呼ばれる1%以下のコモノマーを含むテトラフルオロエチレンの共重合体(変性PTFE)が挙げられる。含フッ素重合体はTFEのホモポリマーであることが好ましい。
変性PTFE水性分散液からなる塵埃抑制処理剤は、PTFE水性分散液からなる塵埃抑制処理剤に比べ塵埃抑制効果が低く、同じ塵埃抑制効果を出すためにしばしば50%以上多い量の処理剤を使用しなければならないことがある。
The fluoropolymer of the present invention includes a tetrafluoroethylene (TFE) homopolymer (PTFE) called a homopolymer and a tetrafluoroethylene copolymer (modified PTFE) containing 1% or less of a comonomer called a modified polymer. ). The fluoropolymer is preferably a TFE homopolymer.
The dust suppression treatment agent composed of the modified PTFE aqueous dispersion has a lower dust suppression effect than the dust suppression treatment agent composed of the PTFE aqueous dispersion, and the amount of the treatment agent used is often 50% or more in order to produce the same dust suppression effect. There are things you have to do.

本発明の含フッ素重合体水性分散液中の含フッ素重合体は、平均粒径0.1〜0.5μm程度、好ましくは0.1〜0.3μm程度のコロイド粒子であることが望ましい。平均粒径が0.1μ未満のコロイド粒子は防塵効果が低く、一方平均粒径が0.5μを越えるコロイド粒子の水性分散液は安定性が低くなる傾向がある。   The fluoropolymer in the fluoropolymer aqueous dispersion of the present invention is desirably a colloidal particle having an average particle size of about 0.1 to 0.5 μm, preferably about 0.1 to 0.3 μm. Colloidal particles having an average particle size of less than 0.1 μm have a low dustproof effect, while aqueous dispersions of colloidal particles having an average particle size of more than 0.5μ tend to be less stable.

また、比重は2.27以下、好ましくは2.22以下、より好ましくは2.20以下であることが望ましい。比重が2.27を越えるポリテトラフルオロエチレンも防塵効果が低くなる傾向がある。   The specific gravity is 2.27 or less, preferably 2.22 or less, more preferably 2.20 or less. Polytetrafluoroethylene having a specific gravity exceeding 2.27 also tends to have a low dustproof effect.

本発明の含フッ素重合体水性分散液中の含フッ素重合体濃度は特に限定されないが、塵埃発生物質への含フッ素重合体の分散効果を高めるためには、その濃度が低いほど好ましい。一方、含フッ素重合体水性分散液を輸送する際にはその濃度が高いほど輸送コストを節約できるため、通常10重量%以上、好ましくは20〜70重量%の範囲であることが望ましい。更に高い濃度は含フッ素重合体水性分散液の安定性を損ねるため好ましくない。従って、製品として販売される塵埃抑制処理剤組成物中の含フッ素重合体濃度は、20〜70重量%であり、塵埃発生物質へ混合するときはそれを水で希釈して5重量%以下の含フッ素重合体濃度として使用することも可能である。   The concentration of the fluoropolymer in the aqueous fluoropolymer dispersion of the present invention is not particularly limited, but in order to enhance the effect of dispersing the fluoropolymer in the dust generating substance, the lower the concentration, the better. On the other hand, when the fluoropolymer aqueous dispersion is transported, the higher the concentration, the more the transportation cost can be saved. Therefore, it is usually 10% by weight or more, preferably 20 to 70% by weight. A higher concentration is not preferable because it impairs the stability of the aqueous fluoropolymer dispersion. Accordingly, the concentration of the fluoropolymer in the dust control agent composition sold as a product is 20 to 70% by weight, and when mixed into a dust generating substance, it is diluted with water to 5% by weight or less. It can also be used as the fluoropolymer concentration.

本発明の含フッ素重合体水性分散液の含フッ素乳化剤は、難分解性であり環境への蓄積が懸念されるので含有率は低いことが望まれ、実用的な除去方法で含フッ素乳化剤の安定した含有率での製造が可能な50ppm以下であることが好ましい。   The fluorine-containing emulsifier of the fluoropolymer aqueous dispersion of the present invention is hardly decomposable and is likely to accumulate in the environment, so it is desired that the content is low. It is preferable that it is 50 ppm or less that can be produced at a reduced content.

本発明の含フッ素乳化剤の含有率が50ppm以下である含フッ素重合体水性分散液を得る方法には特に制限がないが、例えば米国特許第2,559,752号に開示されているような乳化重合法、即ちテトラフルオロエチレンを水溶性重合開始剤及び乳化剤としてフルオロアルキル基を疎水基とするアニオン系界面活性剤(含フッ素乳化剤)を含む水性媒体中に圧入、重合して得られる、含フッ素乳化剤(アンモニウム塩及び/又はアルカリ塩の形のパーフルオロオクタン酸)を含フッ素重合体の重量に対し約0.02〜1重量%含む水性分散液から、含フッ素乳化剤を公知の除去方法、例えば特表2005−501956号(WO 2003/020836)及び特表2002−532583号(WO 00/35971)に記載される有効量の陰イオン交換体と接触させ分離して除去する方法、或いは米国特許第4,369,226号に記載される含フッ素重合体水性分散液の限外ろ過により除去する方法、にて除去することにより得ることができる。含フッ素乳化剤の除去方法はこれらに限定されるものではない。   There is no particular limitation on the method for obtaining the aqueous fluoropolymer dispersion in which the content of the fluoroemulsifier of the present invention is 50 ppm or less. For example, emulsification as disclosed in US Pat. No. 2,559,752 Fluorine-containing polymer obtained by injecting and polymerizing in an aqueous medium containing a polymerization method, that is, an aqueous surfactant containing tetrafluoroethylene as a water-soluble polymerization initiator and an anionic surfactant having a fluoroalkyl group as a hydrophobic group (fluorine-containing emulsifier). A known method for removing a fluorine-containing emulsifier from an aqueous dispersion containing about 0.02 to 1% by weight of an emulsifier (perfluorooctanoic acid in the form of an ammonium salt and / or an alkali salt) based on the weight of the fluorine-containing polymer, for example, Included in JP 2005-501956 (WO 2003/020836) and JP 2002-532583 (WO 00/35971) Removal by contact with an effective amount of anion exchanger and separation or removal by ultrafiltration of fluoropolymer aqueous dispersion described in US Pat. No. 4,369,226 Can be obtained. The method for removing the fluorine-containing emulsifier is not limited to these.

PTFE水性分散液に乳化剤として含まれる界面活性剤(含フッ素乳化剤)は、重合における反応不活性の故に不可欠のものではあるが難分解性で環境への影響が懸念されるため、塵埃抑制処理剤から出来るだけ除去されることが望ましい。また、含フッ素乳化剤は高価であるため回収され再利用されることが望ましい。   A surfactant (fluorinated emulsifier) contained as an emulsifier in an aqueous PTFE dispersion is indispensable because of reaction inactivity in polymerization, but it is difficult to decompose and there is a concern about the influence on the environment. It is desirable to remove as much as possible. Moreover, since the fluorine-containing emulsifier is expensive, it is desirable to collect and reuse it.

前記した本発明の含フッ素重合体水性分散液を得る乳化重合法において、乳化剤としては米国特許第2,559,752号に開示されている乳化剤を選択して使用することができるが、本発明の目的のためには、特に非テロゲン性乳化剤と呼ばれることがある乳化剤が好ましく、たとえば炭素数6〜20程度、好ましくは炭素数6〜12程度のF(CF(CHCOOH(m:0または1、n:6〜20)で表されるフッ素含有アルカン酸またはその塩、フッ素含有アルキルスルホン酸またはその塩などを挙げることができる。塩としては、アルカリ金属塩、アンモニウム塩、アミン塩などを挙げることができる。具体的には、パーフルオロヘプタン酸、パーフルオロオクタン酸、及びそれらの塩、2−パーフルオロヘキシルエタンスルホン酸及びその塩などを挙げることができるがこれに限られるものではない。 In the emulsion polymerization method for obtaining the fluoropolymer aqueous dispersion of the present invention described above, the emulsifier disclosed in US Pat. No. 2,559,752 can be selected and used as the emulsifier. For this purpose, emulsifiers that are sometimes called non-telogenic emulsifiers are preferred, for example, F (CF 2 ) n (CH 2 ) m COOH having about 6 to 20 carbon atoms, preferably about 6 to 12 carbon atoms. The fluorine-containing alkanoic acid represented by (m: 0 or 1, n: 6-20) or its salt, the fluorine-containing alkylsulfonic acid or its salt, etc. can be mentioned. Examples of the salt include alkali metal salts, ammonium salts, and amine salts. Specific examples include perfluoroheptanoic acid, perfluorooctanoic acid, and salts thereof, 2-perfluorohexylethanesulfonic acid, and salts thereof, but are not limited thereto.

更に、本発明の含フッ素重合体水性分散液は、含フッ素重合体水性分散液の安定性を高めるため乳化安定剤を含んでいてもよい。乳化安定剤としては、炭化水素系アニオン系界面活性剤が好ましい。この界面活性剤は本質的に土中成分であるカルシウム、アルミニウム及び鉄分と水に不溶性又は難溶性の塩を形成するため、界面活性剤に起因する河川、湖沼及び地下水汚染を回避することができる。   Furthermore, the fluoropolymer aqueous dispersion of the present invention may contain an emulsion stabilizer in order to improve the stability of the fluoropolymer aqueous dispersion. As the emulsion stabilizer, a hydrocarbon-based anionic surfactant is preferable. This surfactant forms a salt that is insoluble or sparingly soluble in water with calcium, aluminum and iron, which are essentially components in the soil, thus avoiding river, lake and groundwater contamination caused by the surfactant. .

このような炭化水素系アニオン系界面活性剤としては、高級脂肪酸塩類、高級アルコール硫酸エステル塩類、液体脂肪油硫酸エステル塩類、脂肪族アルコールリン酸エステル塩類、二塩基性脂肪酸エステルスルホン酸塩類、アルキルアリルスルホン酸塩類などがあるが、特にポリオキシエチレンアルキルフェニルエーテルエチレンスルホン酸(ポリオキシエチレンのnは1〜6、アルキルの炭素数は8〜11)、アルキルベンゼンスルホン酸(アルキルの炭素数は10〜12)及び、ジアルキルスルホコハク酸エステル(アルキルの炭素数は8〜10)などのNa、K、Li、及びNH塩はPTFE水性エマルジョンに高い機械的安定性を与えるため、好ましいものとして例示することが出来る。 Examples of such hydrocarbon anionic surfactants include higher fatty acid salts, higher alcohol sulfate esters, liquid fatty oil sulfate esters, aliphatic alcohol phosphate esters, dibasic fatty acid ester sulfonates, alkyl allyls. Although there are sulfonates, etc., in particular, polyoxyethylene alkylphenyl ether ethylene sulfonic acid (wherein polyoxyethylene n is 1 to 6, alkyl has 8 to 11 carbon atoms), alkylbenzene sulfonic acid (alkyl has 10 to 10 carbon atoms). 12) and Na, K, Li, and NH 4 salts such as dialkylsulfosuccinic acid esters (wherein the alkyl has 8 to 10 carbon atoms) give high mechanical stability to the aqueous PTFE emulsion, and should be exemplified as preferred. I can do it.

乳化安定剤の添加量はPTFEの重量当り1.0重量%以上であり、好ましくは1.5〜5重量%の範囲である。1.0重量%未満の添加量では含フッ素重合体水性分散液の安定効果が低く、また10重量%以上の添加量では経済的に不利である。   The addition amount of the emulsion stabilizer is 1.0% by weight or more per weight of PTFE, preferably in the range of 1.5 to 5% by weight. When the addition amount is less than 1.0% by weight, the effect of stabilizing the fluoropolymer aqueous dispersion is low, and when the addition amount is 10% by weight or more, it is economically disadvantageous.

本発明の塵埃抑制処理剤組成物は、含フッ素重合体を発塵性物質と混合し、該混合物に約20〜200℃の温度で圧縮−せん断作用を施すことによりポリテトラフルオロエチレンをフィブリル化して発塵性物質の塵埃を抑制する方法、例えば特許第2827152号、特許第2538783号等の方法において、用いられることが好ましい。   The dust control agent composition of the present invention fibrillates polytetrafluoroethylene by mixing a fluoropolymer with a dusting substance and subjecting the mixture to a compression-shearing action at a temperature of about 20 to 200 ° C. Therefore, it is preferably used in a method for suppressing dust of a dust-generating substance, for example, a method such as Japanese Patent No. 2827152, Japanese Patent No. 2538783 and the like.

また、本発明の塵埃抑制処理剤組成物は、特開2000-185956号、特開2000−185959号、及び特開2002−60738号に記載されるフィブリル化性PTFEとして用いることができる。   Moreover, the dust suppressing treatment agent composition of the present invention can be used as a fibrillating PTFE described in JP-A No. 2000-185556, JP-A No. 2000-185959, and JP-A No. 2002-60738.

本発明において塵埃抑制処理される発塵性粉末状物質は、無機及び/または有機の発塵性物質であって、物質、形状などには特に限定はない。本発明は、発塵性物質として発塵性粉末状物質にも効果的に適用できる。特に好適な発塵性物質としては、生産量が多く、船舶、貨車又は自動車などにより大量輸送が行われるような発塵性物質であって、例えば、セメント粉、消石灰粉、生石灰粉、炭酸カルシウム粉、スラグ粉、フライアッシュ、石膏、粒子状金属などが挙げられる。更に、滑石(タルク)、珪石(シリカ)、カーボンブラック、各種活性炭、粘土、金属酸化物、及び顔料などの各種充填材が挙げられる。   In the present invention, the dust generating powdery substance to be subjected to dust suppression treatment is an inorganic and / or organic dust generating substance, and the substance, shape, etc. are not particularly limited. The present invention can also be effectively applied to a dusting powdery substance as a dusting substance. Particularly suitable dust generating materials are dust generating materials that are produced in large quantities and are transported in large quantities by ships, freight cars or automobiles. For example, cement powder, slaked lime powder, quick lime powder, calcium carbonate Examples thereof include powder, slag powder, fly ash, gypsum, and particulate metal. Furthermore, various fillers, such as talc, talc, silica, carbon black, various activated carbons, clay, metal oxides, and pigments, can be mentioned.

本発明の塵埃抑制処理剤は、建材分野、土壌安定材分野、固化材分野、肥料分野、焼却灰及び有害物質の埋立処分分野、防爆分野、化粧品分野等の塵埃抑制処理に好適に用いられる。   The dust suppressing treatment agent of the present invention is suitably used for dust suppressing treatment in the building material field, soil stabilizing material field, solidifying material field, fertilizer field, incineration ash and hazardous substance landfill disposal field, explosion-proof field, cosmetic field, and the like.

以下に本発明を、実施例および比較例を挙げてさらに具体的に説明するが、この説明が本発明を限定するものではない。   The present invention will be described more specifically with reference to examples and comparative examples below, but this description does not limit the present invention.

本発明において各物性の測定は、下記の方法によって行った。
(1)含フッ素重合体粒子の平均粒子径
含フッ素重合体粒子の平均粒径は、マイクロトラックUPA150 Model No.9340(日機装社製)を用いて測定した。
(2)発塵性粉体の粒子径
(株)堀場製作所製レーザー回折/散乱式粒度分布測定器にて、エタノールを分散媒として測定した。
In the present invention, each physical property was measured by the following method.
(1) Average particle diameter of fluoropolymer particles The average particle diameter of the fluoropolymer particles was measured by Microtrac UPA150 Model No. It measured using 9340 (made by Nikkiso Co., Ltd.).
(2) Particle size of dust generating powder Using a laser diffraction / scattering particle size distribution measuring instrument manufactured by Horiba, Ltd., ethanol was measured as a dispersion medium.

(3)含フッ素重合体の標準比重
ASTM D−4894により測定した。
乳化重合により得られるPTFE水性分散体を、純水を用いて15重量%濃度に調整する。その後ポリエチレン容器(1000ml容量)に約750ml入れ手で激しく振蕩して重合体を凝集させる。水から分離した重合体のパウダーを150℃で16時間乾燥する。乾燥した樹脂粉末12.0gを直径2.85cmの円筒形型中に入れてならし、30秒後に最終圧力が350kg/cmとなるよう圧力を次第に増加し、350kg/cmの最終圧力で2分間保持する。このようにして得られた予備成形体を30分間380℃の空気炉中で焼成した後、1分間1℃の割合で294℃まで冷却し、294℃で1分間保持した後、空気炉中から取り出し室温(23±1℃)で冷却して標準試料とする。室温(23℃±1℃)における同体積の水の重量に対する標準試料の重量比を標準比重とする。
この標準比重は平均分子量の目安となり、一般に標準比重が低い程分子量は大きい。
(3) Standard specific gravity of fluoropolymer Measured by ASTM D-4894.
The PTFE aqueous dispersion obtained by emulsion polymerization is adjusted to a concentration of 15% by weight using pure water. Thereafter, the polymer is aggregated by vigorously shaking about 750 ml in a polyethylene container (1000 ml capacity). The polymer powder separated from the water is dried at 150 ° C. for 16 hours. The dried resin powder 12.0g break were placed in cylindrical mold having a diameter of 2.85Cm, gradually increasing the pressure to a final pressure becomes 350 kg / cm 2 after 30 seconds, at a final pressure of 350 kg / cm 2 Hold for 2 minutes. The preform thus obtained was fired in an air furnace at 380 ° C. for 30 minutes, cooled to 294 ° C. at a rate of 1 ° C. for 1 minute, held at 294 ° C. for 1 minute, and then from the air furnace. Take out and cool at room temperature (23 ± 1 ° C.) to make a standard sample. The weight ratio of the standard sample to the weight of the same volume of water at room temperature (23 ° C. ± 1 ° C.) is defined as the standard specific gravity.
This standard specific gravity is a measure of the average molecular weight. In general, the lower the standard specific gravity, the higher the molecular weight.

(4)フッ素樹脂水性分散液中の含フッ素乳化剤濃度
フッ素樹脂水性分散液を−20℃の冷凍庫に入れ凍らせ、含フッ素重合体を凝集し水と分離した。ポリ容器の中身を全てソックスレーの抽出器に移し、約80mlのメタノールで7時間抽出を行う。
抽出に用いたメタノールをエバポレーターで蒸留し50ml以下に濃縮する。濃縮したメタノールを50mlのメスフラスコに入れて純水でメスアップする。メスアップしたサンプル液を液体クロマトグラフにかけて測定を行い、フッ素樹脂水性分散液中の含フッ素乳化剤濃度を算出する。
(4) Concentration of fluorinated emulsifier in fluororesin aqueous dispersion The fluororesin aqueous dispersion was frozen in a −20 ° C. freezer, and the fluoropolymer was aggregated and separated from water. Transfer the entire contents of the plastic container to a Soxhlet extractor and extract with about 80 ml of methanol for 7 hours.
Methanol used for extraction is distilled with an evaporator and concentrated to 50 ml or less. Concentrated methanol is placed in a 50 ml volumetric flask and diluted with pure water. The sample solution that has been made up is subjected to a liquid chromatograph for measurement, and the concentration of the fluorinated emulsifier in the aqueous fluororesin dispersion is calculated.

(5)落下粉塵量
内径39cm、高さ59cmの円筒容器の頂部投入口より試料200gを自然落下させ、底面より高さ45cmの位置の容器内の浮遊粉塵量(相対濃度(CPM:Count per Minute)を散乱光式デジタル粉塵計により測定する。浮遊粉塵量の測定は、試料投入後1分間計測を連続し5回行い、試料投入前の測定値(ダークカウント)を差し引いた値の幾何平均値を当該試料の「落下粉塵量」とする。幾何平均値xは次の式により求める。
Log x=1/5・Σlog(xi‐d)
ここで、xi:個々の浮遊粉塵量、d:ダークカウントである。
(5) Amount of falling dust 200 g of the sample is naturally dropped from the top inlet of a cylindrical container having an inner diameter of 39 cm and a height of 59 cm, and the amount of suspended dust (relative concentration (CPM: Count per minute) in the container at a height of 45 cm from the bottom. ) Is measured with a scattered-light digital dust meter, and the amount of airborne dust is measured five times for 1 minute after the sample is added, and the geometric average value obtained by subtracting the measured value (dark count) before the sample is added. Is the “falling dust amount.” The geometric mean value x is determined by the following equation.
Log x = 1/5 · Σlog (xi-d)
Here, xi: individual suspended dust amount, d: dark count.

(原料)
本発明実施例および比較例で用いた原料は下記のとおりである。
(1)PTFE水性分散液(I)
(平均粒径0.2μm、樹脂固形分濃度30重量%、含フッ素乳化剤含有量21ppm、比重2.19、アニオン系界面活性剤をPTFEの重量に対して3.5重量%含む)
(2)PTFE水性分散液(II)
(三井デュポンフロロケミカル製、312−J、含フッ素乳化剤含有量1040ppm、比重2.19、アニオン系界面活性剤をPTFEの重量に対して3.0重量%含む)
(3)粉末生石灰
(CaO93.5%、MgO4.2%)
300μmの標準網フルイを全通、150μmの標準網フルイ残分0.04%、90μmの標準網フルイ残分0.17%、90μmの標準網フルイ通過分99.83%の粉末生石灰
(4)普通ポルトランドセメント (太平洋セメント製)
(5)II型無水石膏 (平均粒子径9.0μm、最大粒子径101μm)
(6)高炉水砕スラグ粉末(平均粒子径8.9μm、最大粒子径100μm)
(material)
The raw materials used in the examples and comparative examples of the present invention are as follows.
(1) PTFE aqueous dispersion (I)
(Average particle size 0.2 μm, resin solid content concentration 30 wt%, fluorine-containing emulsifier content 21 ppm, specific gravity 2.19, anionic surfactant is included 3.5 wt% with respect to the weight of PTFE)
(2) PTFE aqueous dispersion (II)
(Mitsui DuPont Fluorochemicals, 312-J, fluorine-containing emulsifier content 1040 ppm, specific gravity 2.19, containing 3.0% by weight of anionic surfactant based on the weight of PTFE)
(3) Powdered quicklime (CaO 93.5%, MgO 4.2%)
Powdered lime with a 300 μm standard mesh screen throughout, 150 μm standard screen screen residue 0.04%, 90 μm standard screen screen residue 0.17%, 90 μm standard screen screen through 99.83% Normal Portland cement (manufactured by Taiheiyo Cement)
(5) Type II anhydrous gypsum (average particle size 9.0 μm, maximum particle size 101 μm)
(6) Granulated blast furnace slag powder (average particle size 8.9 μm, maximum particle size 100 μm)

(実施例1)
粉末生石灰1,000gを容積5リットルの小型ソイルミキサーに投入し、回転数140r.p.m.で攪拌しながら、PTFE水性分散液(I)1.67g(生石灰に対しPTFE樹脂固形分0.05質量%に相当)を清水98.8gに分散した分散液を徐々に投入した。
投入開始より約1分後には生石灰の水和反応熱による水蒸気を発生し始め、その後約2分で水分のすべてが生石灰の水和により消石灰の生成のため使用され尽くし水蒸気の発生が無くなった。攪拌開始より5分後にミキサーの攪拌を止めた。このときの温度を水銀温度計で計測すると95℃であった。この塵埃抑制処理された生石灰は、水和反応により新たに生成した消石灰約30%を含む生石灰と消石灰の混合物であった。塵埃抑制処理された生石灰の落下粉塵量を測定した。結果を表1に示す。
Example 1
1. 1,000 g of powdered quicklime was put into a small soil mixer having a volume of 5 liters and stirred at a rotational speed of 140 rpm, 1.67 g of PTFE aqueous dispersion (I) (PTFE resin solid content 0. (Corresponding to 05% by mass) was gradually added to a dispersion of 98.8 g of fresh water.
About 1 minute after the start of charging, steam started to be generated due to the heat of hydration reaction of quick lime, and after about 2 minutes, all of the water was used up for the production of slaked lime due to the hydration of quick lime, and the generation of water vapor was eliminated. After 5 minutes from the start of stirring, stirring of the mixer was stopped. The temperature at this time was 95 ° C. when measured with a mercury thermometer. The quicklime subjected to the dust suppression treatment was a mixture of quicklime and slaked lime containing about 30% of slaked lime newly generated by a hydration reaction. The amount of falling dust of the quicklime that had been dust-suppressed was measured. The results are shown in Table 1.

(実施例2)
PTFE水分散液(I)1.00g(生石灰に対しPTFE樹脂固形分0.03質量%に相当)を清水99.3gに分散した分散液を用いた以外は、実施例1と同様にして塵埃抑制処理された生石灰を得た。得られた塵埃抑制処理された生石灰の落下粉塵量を測定した。結果を表1に示す。
(Example 2)
Dust in the same manner as in Example 1 except that a dispersion obtained by dispersing 1.00 g of PTFE aqueous dispersion (I) (corresponding to 0.03% by mass of PTFE resin solid content with respect to quicklime) in 99.3 g of fresh water was used. Inhibited quick lime was obtained. The amount of falling dust of the obtained quick lime subjected to the dust suppression treatment was measured. The results are shown in Table 1.

(実施例3)
生石灰の水和反応熱を利用して普通ポルトランドセメント(発塵性粉体)を加温し、塵埃抑制処理する方法である。
粉末生石灰100gを容積5リットルの小型ソイルミキサーに投入し、回転数140r.p.m.で攪拌しながら、PTFE水性分散液(I)1.67g(生石灰に対しPTFE樹脂固形分0.05質量%に相当)を清水35.0gに分散した分散液を徐々に投入した。
投入開始より約1分後には生石灰の水和反応熱による水蒸気を発生し始め、その後約2分で水分のすべてが生石灰の水和により消石灰の生成のため使用され尽くし水蒸気の発生が無くなった。攪拌開始より5分後にミキサーの攪拌を止めた。このときの温度を水銀温度計で計測すると95℃であった。塵埃抑制処理された生石灰は、水和反応により新たに生成した消石灰を含む生石灰と消石灰の団子状の混合物であった。
(Example 3)
This is a method of heating dust from ordinary Portland cement (dust generating powder) using the heat of hydration reaction of quicklime and performing dust suppression treatment.
100 g of powdered quicklime was put into a small soil mixer having a volume of 5 liters and stirred at a rotational speed of 140 rpm, 1.67 g of PTFE aqueous dispersion (I) (PTFE resin solid content 0.05 mass relative to quicklime) %) Was gradually added to 35.0 g of fresh water.
About 1 minute after the start of charging, steam started to be generated due to the heat of hydration reaction of quick lime, and after about 2 minutes, all of the water was used up for the production of slaked lime due to the hydration of quick lime, and the generation of water vapor was eliminated. After 5 minutes from the start of stirring, stirring of the mixer was stopped. The temperature at this time was 95 ° C. when measured with a mercury thermometer. The quicklime subjected to the dust suppression treatment was a dumpling mixture of quicklime and slaked lime containing slaked lime newly generated by a hydration reaction.

これをマスターバッチのマスターとして、小型ソイルミキサー(回転数140r.p.m.)で攪拌しながら、普通ポルトランドセメント900gを徐々に投入した。普通ポルトランドセメントセメント投入後、約5分でミキサーの攪拌を止めた。このときの温度を水銀温度計で計測すると57℃であった。この塵埃抑制処理された普通ポルトランドセメントの落下粉塵量を測定した。結果を表1に示す。   Using this as a master of the master batch, 900 g of ordinary Portland cement was gradually added while stirring with a small soil mixer (rotation speed 140 rpm). Mixing of ordinary Portland cement was stopped after about 5 minutes. The temperature at this time was 57 ° C. when measured with a mercury thermometer. The amount of falling dust of the ordinary Portland cement subjected to the dust suppression treatment was measured. The results are shown in Table 1.

(実施例4〜6)
表1に示す発塵性粉体200gを電熱式乾燥機にて予め90℃に加温した。加温した発塵性粉体20gと、表1に示す固形分割合(質量%)のPTFE水性分散液(I)とを、予め90℃の電熱式乾燥機で暖めた容量1リットルのアルミナ性乳鉢中で約5分間混合・攪拌し混合物を得た。得られた混合物をマスターとし、該マスターに加温した発塵性粉体の残り180gを加え約5分間混合・攪拌し、塵埃抑制処理された発塵性粉体を得た。得られた発塵性粉体の落下粉塵量を測定した。結果を表1に示す。
(Examples 4 to 6)
200 g of the dusting powder shown in Table 1 was preheated to 90 ° C. with an electric heating dryer. 20 g of heated dusting powder and a PTFE aqueous dispersion (I) having a solid content ratio (mass%) shown in Table 1 were heated in advance by an electrothermal dryer at 90 ° C. to a volume of 1 liter of alumina. Mixing and stirring for about 5 minutes in a mortar gave a mixture. The obtained mixture was used as a master, and the remaining 180 g of the heated dust generating powder was added to the master and mixed and stirred for about 5 minutes to obtain a dust generating powder subjected to dust suppression treatment. The amount of falling dust of the resulting dusting powder was measured. The results are shown in Table 1.

(比較例1)
生石灰の落下粉塵量を測定した。結果を表1に示す。
(Comparative Example 1)
The amount of falling dust of quicklime was measured. The results are shown in Table 1.

(比較例2)
普通ポルトランドセメントの落下粉塵量を測定した。結果を表1に示す。
(Comparative Example 2)
The amount of falling dust of normal Portland cement was measured. The results are shown in Table 1.

(比較例3)
II型無水石膏の落下粉塵量を測定した。結果を表1に示す。
(Comparative Example 3)
The amount of falling dust of type II anhydrous gypsum was measured. The results are shown in Table 1.

(比較例4)
高炉水砕スラグ粉末の落下粉塵量を測定した。結果を表1に示す。
(Comparative Example 4)
The amount of falling dust of granulated blast furnace slag powder was measured. The results are shown in Table 1.

(参考例1)
PTFE水分散液(II)1.67g(生石灰に対しPTFE樹脂固形分0.05質量%に相当)を清水98.8gに分散した分散液を用いた以外は、実施例1と同様にして塵埃抑制処理された生石灰を得た。得られた塵埃抑制処理された生石灰の落下粉塵量を測定した。結果を表1に示す。
(Reference Example 1)
Dust in the same manner as in Example 1 except that a dispersion in which 1.67 g of PTFE aqueous dispersion (II) (corresponding to a solid content of PTFE resin of 0.05% by weight of quicklime) was dispersed in 98.8 g of fresh water was used. Inhibited quick lime was obtained. The amount of falling dust of the obtained quick lime subjected to the dust suppression treatment was measured. The results are shown in Table 1.

(参考例2)
PTFE水分散液(II)1.00g(生石灰に対しPTFE樹脂固形分0.03質量%に相当)を清水99.3gに分散した分散液を用いた以外は、実施例1と同様にして塵埃抑制処理された生石灰を得た。得られた塵埃抑制処理された生石灰の落下粉塵量を測定した。結果を表1に示す。
(Reference Example 2)
Dust in the same manner as in Example 1 except that 1.00 g of PTFE aqueous dispersion (II) (corresponding to 0.03% by mass of PTFE resin solid content with respect to quicklime) was dispersed in 99.3 g of fresh water. Inhibited quick lime was obtained. The amount of falling dust of the obtained quick lime subjected to the dust suppression treatment was measured. The results are shown in Table 1.

(参考例3〜5)
PTFE水性分散液(II)を用いた以外は、実施例4〜6と同様にして塵埃抑制された発塵性粉体を得た。得られた発塵性粉体の落下粉塵量を測定した。結果を表1に示す。
(Reference Examples 3-5)
Except for using the PTFE aqueous dispersion (II), dust-generating powders with reduced dust were obtained in the same manner as in Examples 4-6. The amount of falling dust of the resulting dusting powder was measured. The results are shown in Table 1.

Figure 2012077312
Figure 2012077312

本発明により、防塵効果が高く、且つ環境問題の可能性が低い含フッ素重合体水性分散液からなる塵埃抑制処理剤が提供される。 According to the present invention, there is provided a dust suppression treatment agent comprising a fluoropolymer aqueous dispersion having a high dustproof effect and a low possibility of environmental problems.

Claims (7)

含フッ素乳化剤の含有率が50ppm以下であるポリテトラフルオロエチレンの水性分散液であって、該ポリテトラフルオロエチレンの比重が2.27以下であって、平均粒径が0.1〜0.5μmであり、乳化安定剤として炭化水素系アニオン系界面活性剤を含有する含フッ素重合体水性分散液からなり、発塵性物質と混合して、該混合物に約20〜200℃の温度で圧縮−剪断作用を施すことにより、ポリテトラフルオロエチレンをフィブリル化して発塵性物質の塵埃を抑制するために使用する塵埃抑制処理剤組成物。 An aqueous dispersion of polytetrafluoroethylene having a fluorine-containing emulsifier content of 50 ppm or less, wherein the polytetrafluoroethylene has a specific gravity of 2.27 or less and an average particle size of 0.1 to 0.5 μm Comprising a fluoropolymer aqueous dispersion containing a hydrocarbon-based anionic surfactant as an emulsion stabilizer , mixed with a dusting substance, and compressed into the mixture at a temperature of about 20 to 200 ° C. A dust suppressing treatment agent composition used for fibrillating polytetrafluoroethylene by applying a shearing action to suppress dust of a dust generating substance. 前記ポリテトラフルオロエチレンの比重が2.22以下である請求項1に記載の塵埃抑制処理剤組成物。   The dust control agent composition according to claim 1, wherein the specific gravity of the polytetrafluoroethylene is 2.22 or less. 前記含フッ素乳化剤が、アニオン系含フッ素乳化剤であることを特徴とする請求項1または2に記載された塵埃抑制処理剤組成物。   The dust-controlling agent composition according to claim 1 or 2, wherein the fluorinated emulsifier is an anionic fluorinated emulsifier. 前記含フッ素重合体水性分散液が、含フッ素乳化剤を用いてテトラフルオロエチレンを重合して得られた重合体水性分散液から、含フッ素乳化剤を除去して得られることを特徴とする請求項1〜3のいずれかに記載の塵埃抑制処理剤組成物。   2. The aqueous fluoropolymer dispersion is obtained by removing a fluoroemulsifier from an aqueous polymer dispersion obtained by polymerizing tetrafluoroethylene using a fluoroemulsifier. The dust suppression processing agent composition in any one of -3. 前記炭化水素系アニオン系界面活性剤が、ポリテトラフルオロエチレンの重量当り1.0重量%以上10重量%未満であることを特徴とする請求項1に記載の発塵性物質の塵埃抑制処理方法。The dust control method for dusting substances according to claim 1, wherein the hydrocarbon-based anionic surfactant is 1.0 wt% or more and less than 10 wt% per weight of polytetrafluoroethylene. . 前記発塵性物質が、セメント粉、消石灰粉、生石灰粉、炭酸カルシウム粉、スラグ粉、フライアッシュ、石膏、粒子状金属、滑石(タルク)、珪石(シリカ)、カーボンブラック、各種活性炭、金属酸化物及び顔料から選ばれたものである請求項1〜5のいずれかに記載の塵埃抑制処理剤組成物。   The dust generating material is cement powder, slaked lime powder, quick lime powder, calcium carbonate powder, slag powder, fly ash, gypsum, particulate metal, talc, silica stone, carbon black, various activated carbons, metal oxidation The dust control agent composition according to any one of claims 1 to 5, wherein the dust control agent composition is selected from products and pigments. 前記塵埃抑制処理剤組成物が、建材分野、土壌安定材分野、固化材分野、肥料分野、焼却灰及び有害物質の埋立処分分野、防爆分野または化粧品分野に用いられる請求項1〜6のいずれかに記載の塵埃抑制処理剤組成物。   The dust control agent composition is used in the building materials field, the soil stabilizer field, the solidified material field, the fertilizer field, the landfill disposal field of incinerated ash and harmful substances, the explosion-proof field, or the cosmetic field. The dust control agent composition as described in 1.
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020105419A (en) * 2018-12-28 2020-07-09 株式会社Nippo Dust suppression processing method
JP2020105417A (en) * 2018-12-28 2020-07-09 三井・ケマーズ フロロプロダクツ株式会社 Ptfe aqueous dispersion, and dust inhibiting agent composition made of the aqueous dispersion
WO2023106288A1 (en) * 2021-12-06 2023-06-15 株式会社Nippo Dust suppression treatment method

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2559752A (en) * 1951-03-06 1951-07-10 Du Pont Aqueous colloidal dispersions of polymers
JPS5232877B2 (en) * 1976-09-17 1977-08-24
JPH0820767A (en) * 1994-07-11 1996-01-23 Murakashi Sekkai Kogyo Kk Method for preventing dusting
JP2002532583A (en) * 1998-12-11 2002-10-02 ダイネオン・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング・ウント・コンパニー・コマンディトゲゼルシャフト Aqueous dispersion of fluoropolymer
WO2003051988A2 (en) * 2001-12-13 2003-06-26 3M Innovative Properties Company Aqueous dispersions of fluoropolymers, method of reducing the fluorine surfactant concentration
JP2005501956A (en) * 2001-09-05 2005-01-20 スリーエム イノベイティブ プロパティズ カンパニー Fluoropolymer dispersion with little or no low molecular weight fluorinated surfactant

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2559752A (en) * 1951-03-06 1951-07-10 Du Pont Aqueous colloidal dispersions of polymers
JPS5232877B2 (en) * 1976-09-17 1977-08-24
JPH0820767A (en) * 1994-07-11 1996-01-23 Murakashi Sekkai Kogyo Kk Method for preventing dusting
JP2002532583A (en) * 1998-12-11 2002-10-02 ダイネオン・ゲゼルシャフト・ミト・ベシュレンクテル・ハフツング・ウント・コンパニー・コマンディトゲゼルシャフト Aqueous dispersion of fluoropolymer
JP2005501956A (en) * 2001-09-05 2005-01-20 スリーエム イノベイティブ プロパティズ カンパニー Fluoropolymer dispersion with little or no low molecular weight fluorinated surfactant
WO2003051988A2 (en) * 2001-12-13 2003-06-26 3M Innovative Properties Company Aqueous dispersions of fluoropolymers, method of reducing the fluorine surfactant concentration

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2020105419A (en) * 2018-12-28 2020-07-09 株式会社Nippo Dust suppression processing method
JP2020105417A (en) * 2018-12-28 2020-07-09 三井・ケマーズ フロロプロダクツ株式会社 Ptfe aqueous dispersion, and dust inhibiting agent composition made of the aqueous dispersion
JP7317307B2 (en) 2018-12-28 2023-07-31 株式会社Nippo Dust suppression treatment method
JP7386610B2 (en) 2018-12-28 2023-11-27 三井・ケマーズ フロロプロダクツ株式会社 PTFE aqueous dispersion and dust suppression treatment agent composition comprising the aqueous dispersion
WO2023106288A1 (en) * 2021-12-06 2023-06-15 株式会社Nippo Dust suppression treatment method

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