JP5786336B2 - Antifoaming agent and method for producing antifoaming agent - Google Patents
Antifoaming agent and method for producing antifoaming agent Download PDFInfo
- Publication number
- JP5786336B2 JP5786336B2 JP2011003431A JP2011003431A JP5786336B2 JP 5786336 B2 JP5786336 B2 JP 5786336B2 JP 2011003431 A JP2011003431 A JP 2011003431A JP 2011003431 A JP2011003431 A JP 2011003431A JP 5786336 B2 JP5786336 B2 JP 5786336B2
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- JP
- Japan
- Prior art keywords
- oil
- antifoaming agent
- alcohol
- emulsion
- petrolatum
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- 238000004519 manufacturing process Methods 0.000 title claims description 8
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- 235000019808 microcrystalline wax Nutrition 0.000 claims description 26
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- 239000004264 Petrolatum Substances 0.000 claims description 21
- 229940066842 petrolatum Drugs 0.000 claims description 21
- 239000000839 emulsion Substances 0.000 claims description 20
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- 235000019512 sardine Nutrition 0.000 description 1
- 229930195734 saturated hydrocarbon Natural products 0.000 description 1
- 150000003333 secondary alcohols Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 235000010413 sodium alginate Nutrition 0.000 description 1
- 239000000661 sodium alginate Substances 0.000 description 1
- 229940005550 sodium alginate Drugs 0.000 description 1
- 239000003549 soybean oil Substances 0.000 description 1
- 235000012424 soybean oil Nutrition 0.000 description 1
- 229940012831 stearyl alcohol Drugs 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- TUNFSRHWOTWDNC-HKGQFRNVSA-N tetradecanoic acid Chemical compound CCCCCCCCCCCCC[14C](O)=O TUNFSRHWOTWDNC-HKGQFRNVSA-N 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 230000008719 thickening Effects 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
- QXJQHYBHAIHNGG-UHFFFAOYSA-N trimethylolethane Chemical compound OCC(C)(CO)CO QXJQHYBHAIHNGG-UHFFFAOYSA-N 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000010698 whale oil Substances 0.000 description 1
- 229920001285 xanthan gum Polymers 0.000 description 1
- 235000010493 xanthan gum Nutrition 0.000 description 1
- 239000000230 xanthan gum Substances 0.000 description 1
- 229940082509 xanthan gum Drugs 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D19/00—Degasification of liquids
- B01D19/02—Foam dispersion or prevention
- B01D19/04—Foam dispersion or prevention by addition of chemical substances
- B01D19/0404—Foam dispersion or prevention by addition of chemical substances characterised by the nature of the chemical substance
Landscapes
- Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Degasification And Air Bubble Elimination (AREA)
- Colloid Chemistry (AREA)
- Paper (AREA)
- Lubricants (AREA)
Description
本発明は、高級アルコールを含む消泡剤、及び消泡剤の製造方法に関する。 The present invention relates to an antifoaming agent containing a higher alcohol and a method for producing the antifoaming agent.
従来、ワックス系消泡剤は、高級アルコール、炭化水素、脂肪酸エステル等の常温で固体又は液体の有効成分を含むO/Wエマルション型である(例えば、特許文献1〜3参照)。しかし、ワックス系消泡剤に対する性能向上の要請は更に高まっており、従来のワックス系消泡剤の改善が必要である。 Conventionally, a wax-type antifoaming agent is an O / W emulsion type containing an active ingredient that is solid or liquid at room temperature, such as higher alcohols, hydrocarbons, and fatty acid esters (for example, see Patent Documents 1 to 3). However, there is a growing demand for improved performance of wax-based antifoaming agents, and improvement of conventional wax-based antifoaming agents is necessary.
ところで、消泡剤による消泡効果は、有効成分自体の性能と、分散した油相の粒子径とによって主に決定される。このため、消泡剤による消泡効果の改善には、有効成分の性能を向上させつつ、分散した油相の粒子径を最適化する必要があるが、油相は容易に凝集しやすく、これらを両立することは困難であった。 By the way, the defoaming effect by the defoaming agent is mainly determined by the performance of the active ingredient itself and the particle diameter of the dispersed oil phase. For this reason, in order to improve the defoaming effect by the antifoaming agent, it is necessary to optimize the particle diameter of the dispersed oil phase while improving the performance of the active ingredient. However, the oil phase easily aggregates, It was difficult to achieve both.
本発明は、以上の実情に鑑みてなされたものであり、油相の凝集が抑制されて消泡効果に優れる消泡剤、及びそのような消泡剤を製造する方法を提供することを目的とする。 The present invention has been made in view of the above circumstances, and an object of the present invention is to provide an antifoaming agent that suppresses aggregation of an oil phase and is excellent in an antifoaming effect, and a method for producing such an antifoaming agent. And
本発明者は、マイクロクリスタリンワックス及び/又はペトロラタムを配合することで有効成分による消泡能力が向上し、それに伴う油相の凝集は、多価アルコールを併用することで抑制されることを見出し、本発明を完成するに至った。具体的に、本発明は以下のものを提供する。 The present inventor has found that the antifoaming ability by the active ingredient is improved by blending microcrystalline wax and / or petrolatum, and the accompanying oil phase aggregation is suppressed by using a polyhydric alcohol together, The present invention has been completed. Specifically, the present invention provides the following.
(1) 高級アルコールと、マイクロクリスタリンワックス及び/又はペトロラタムと、多価アルコールとが配合され、O/Wエマルション構造を有する消泡剤。 (1) An antifoaming agent having an O / W emulsion structure, in which a higher alcohol, microcrystalline wax and / or petrolatum, and a polyhydric alcohol are blended.
(2) 高級アルコールとマイクロクリスタリンワックス及び/又はペトロラタムとを含む液状の油剤を、多価アルコールの存在下で、水へと乳化させてO/Wエマルションを生成する乳化工程を有する消泡剤の製造方法。 (2) An antifoaming agent having an emulsifying step of emulsifying a liquid oil containing a higher alcohol and microcrystalline wax and / or petrolatum into water in the presence of a polyhydric alcohol to produce an O / W emulsion. Production method.
(3) 前記乳化工程の後に、
前記乳化工程より穏やかな撹拌を行い、又は撹拌を行わず、前記O/Wエマルションを常温よりも高い所定温度まで冷却する第1冷却工程と、
その後、第1冷却工程より激しい撹拌を行いながら、前記O/Wエマルションを常温へと冷却する第2冷却工程と、を更に有する(2)記載の製造方法。
(3) After the emulsification step,
A first cooling step in which the O / W emulsion is cooled to a predetermined temperature higher than room temperature without gentle stirring or stirring than the emulsification step;
Then, the 2nd cooling process of cooling the said O / W emulsion to normal temperature, stirring more intensely than a 1st cooling process, The manufacturing method of (2) description.
本発明によれば、マイクロクリスタリンワックス及び/又はペトロラタムを配合することで有効成分による消泡能力が向上し、それに伴う油相の凝集は、多価アルコールを併用することで抑制される。これにより、油相の凝集が抑制されて消泡効果に優れる消泡剤を製造することができる。 According to the present invention, the defoaming ability of the active ingredient is improved by blending microcrystalline wax and / or petrolatum, and the accompanying aggregation of the oil phase is suppressed by using a polyhydric alcohol together. Thereby, the aggregation of an oil phase is suppressed and the antifoamer which is excellent in the defoaming effect can be manufactured.
以下、本発明の実施形態を説明するが、これらが本発明を限定するものではない。 Hereinafter, although embodiment of this invention is described, these do not limit this invention.
本発明に係る消泡剤は、高級アルコールと、マイクロクリスタリンワックス及び/又はペトロラタムと、多価アルコールとが配合され、O/Wエマルション構造を有する。マイクロクリスタリンワックス及び/又はペトロラタムが有効成分による消泡能力を向上し、それに伴う油相の凝集は多価アルコールが抑制する。これにより、油相の凝集が抑制されて消泡効果に優れる消泡剤を製造することができる。 The antifoaming agent according to the present invention contains a higher alcohol, microcrystalline wax and / or petrolatum, and a polyhydric alcohol, and has an O / W emulsion structure. Microcrystalline wax and / or petrolatum improve the defoaming ability of the active ingredient, and the polyhydric alcohol suppresses the accompanying oil phase aggregation. Thereby, the aggregation of an oil phase is suppressed and the antifoamer which is excellent in the defoaming effect can be manufactured.
高級アルコールは、従来、消泡剤において使用されている高級アルコールであってよく、例えば12〜30個、好ましくは18〜30の炭素原子を有する天然アルコールおよび/または合成アルコールの1種以上であってよい。天然アルコールとしては、ラウリルアルコール、ミリスチルアルコール、セチルアルコール、ステアリルアルコール、エイコサノール、ドコサノール、テトラコサノール、ヘキサコサノール、オクタコサノール、ミリシルアルコール等の飽和アルコール、オレイルアルコール等の不飽和アルコールが挙げられる。合成アルコールとしては、チーグラー法で合成された直鎖で非分岐状の飽和アルコール、オキソ法で合成された直鎖第1級アルコールあるいは分岐第1級アルコール、またはこれらの炭素数の異なるアルコール混合物、パラフィンを空気酸化して得られる直鎖第2級アルコール等が挙げられる。高級アルコールの配合量も特に限定されず、消泡剤中の固形成分に対し30〜90質量%程度であってよい。 The higher alcohol may be a higher alcohol conventionally used in an antifoaming agent, for example, one or more of natural alcohols and / or synthetic alcohols having 12 to 30, preferably 18 to 30 carbon atoms. It's okay. Examples of the natural alcohol include lauryl alcohol, myristyl alcohol, cetyl alcohol, stearyl alcohol, eicosanol, docosanol, tetracosanol, hexacosanol, octacosanol and unsaturated alcohol such as oleyl alcohol. Synthetic alcohols include linear, unbranched saturated alcohols synthesized by the Ziegler method, linear primary alcohols or branched primary alcohols synthesized by the oxo method, or mixtures of these alcohols having different carbon numbers, Examples include linear secondary alcohols obtained by air oxidation of paraffin. The blending amount of the higher alcohol is not particularly limited, and may be about 30 to 90% by mass with respect to the solid component in the antifoaming agent.
マイクロクリスタリンワックス及びペトロラタムは、その一方のみ、あるいは組み合わせて配合されてよい。マイクロクリスタリンワックス及びペトロラタムは、パラフィンワックスとともに石油ワックスに属し、本発明ではJISに準拠して石油ワックスを次のように分類する。
パラフィンワックスは、減圧蒸留流出油から分離精製され、常温において固形(融点約50〜70℃)のワックスであり、直鎖状炭化水素を主体とする飽和炭化水素で構成され、油分の含有量が少ない(1%以下)。
マイクロクリスタリンワックスは、減圧蒸留残渣油または重質流出油より分離精製され、常温において固形のワックスであり、パラフィンワックスより高沸点(融点は約60〜90℃)であり、油分含有量が2〜5%である。
ペトロラタムは、減圧蒸留残渣より分離精製され、常温において半固形のワックスであり、マイクロクリスタリンワックスよりも油分が10%程度多い。
The microcrystalline wax and petrolatum may be blended alone or in combination. Microcrystalline wax and petrolatum belong to petroleum wax together with paraffin wax. In the present invention, petroleum wax is classified as follows in accordance with JIS.
Paraffin wax is a wax that is separated and refined from reduced-pressure distilled spilled oil and is solid (melting point: about 50 to 70 ° C.) at room temperature, and is composed of saturated hydrocarbons mainly composed of linear hydrocarbons, and has an oil content of Less (1% or less).
Microcrystalline wax is separated and purified from vacuum distillation residue oil or heavy spilled oil, is a solid wax at normal temperature, has a boiling point higher than that of paraffin wax (melting point is about 60 to 90 ° C.), and has an oil content of 2 to 2. 5%.
Petrolatum is separated and purified from a vacuum distillation residue, is a semi-solid wax at room temperature, and has about 10% more oil than microcrystalline wax.
マイクロクリスタリンワックス及びペトロラタムは、いずれも、微結晶性のワックスで、かつ多価不飽和を有する炭化水素であるため、パラフィンワックス等の一般的なワックスより親水性が高く、消泡剤粒子の泡膜への侵入を容易にするという作用を呈する。このため、有効成分による消泡能力を向上することができる。マイクロクリスタリンワックス及びペトロラタムの配合量は、特に限定されないが、合量で消泡剤中の固形成分に対し5〜50質量%であってよい。なお、パラフィンワックスは、マイクロクリスタリンワックス及び/又はペトロラタムが含まれる限りにおいて、含まれても、含まれていなくてもよい。 Since microcrystalline wax and petrolatum are both microcrystalline waxes and hydrocarbons having polyunsaturation, they are more hydrophilic than general waxes such as paraffin wax, and foam of antifoamer particles. It exhibits the effect of facilitating penetration into the membrane. For this reason, the defoaming ability by an active ingredient can be improved. The blending amount of the microcrystalline wax and petrolatum is not particularly limited, but may be 5 to 50% by mass with respect to the solid component in the antifoaming agent. Paraffin wax may or may not be included as long as microcrystalline wax and / or petrolatum are included.
多価アルコールは、1分子中に2つ以上の水酸基(−OH)を有する化合物である。特に限定されないが、エチレングリコール、ジエチレングリコール等の低分子量ポリエチレングリコール、プロピレングリコール、ジプロピレングリコール等の低分子量ポリプロピレングリコール、その他グリコール類、グリセリン及びその多量体、1,3−プロパンジオール、1,4−ブタンジオール等のアルキレンポリオール等が挙げられる。多価アルコールの分子量も特に限定されず、例えば500以下であってよい。 The polyhydric alcohol is a compound having two or more hydroxyl groups (—OH) in one molecule. Although not particularly limited, low molecular weight polyethylene glycols such as ethylene glycol and diethylene glycol, low molecular weight polypropylene glycols such as propylene glycol and dipropylene glycol, other glycols, glycerin and its multimers, 1,3-propanediol, 1,4- Examples include alkylene polyols such as butanediol. The molecular weight of the polyhydric alcohol is not particularly limited, and may be, for example, 500 or less.
多価アルコールの配合量は、特に限定されないが、消泡剤に対し0.5質量%以上10質量%以下であってよい。また、多価アルコールはマイクロクリスタリンワックス及びペトロラタムによる油相の凝集を抑制する作用を有することから、多価アルコールの配合量はマイクロクリスタリンワックス及びペトロラタムとの相対量で規定されてもよい。つまり、多価アルコールの配合量がマイクロクリスタリンワックス及び/又はペトロラタムの合量に対し過小であると、油相の凝集抑制が十分に得られにくく、過大であっても、油相の凝集抑制が飽和し、経済的でない。そこで、マイクロクリスタリンワックス及び/又はペトロラタムの合量100質量部に対する多価アルコールの配合量の下限は10質量部であることが好ましく、より好ましくは50質量部であり、上限は200質量部であることが好ましく、より好ましくは100質量部である。 Although the compounding quantity of a polyhydric alcohol is not specifically limited, 0.5 mass% or more and 10 mass% or less may be sufficient with respect to an antifoamer. Moreover, since polyhydric alcohol has the effect | action which suppresses aggregation of the oil phase by microcrystalline wax and petrolatum, the compounding quantity of polyhydric alcohol may be prescribed | regulated by the relative amount with microcrystalline wax and petrolatum. That is, if the blending amount of the polyhydric alcohol is too small relative to the total amount of the microcrystalline wax and / or petrolatum, it is difficult to sufficiently suppress the aggregation of the oil phase, and even if it is excessive, the aggregation of the oil phase is suppressed. Saturated and not economical. Therefore, the lower limit of the blending amount of the polyhydric alcohol with respect to 100 parts by mass of the total amount of the microcrystalline wax and / or petrolatum is preferably 10 parts by mass, more preferably 50 parts by mass, and the upper limit is 200 parts by mass. It is preferably 100 parts by mass.
本発明に係る消泡剤は、必要に応じて、炭化水素、脂肪酸エステル、脂肪族ケトン、脂肪族エーテル等の常温で固体又は液体の有効成分を更に含んでもよい。 The antifoaming agent according to the present invention may further contain an active ingredient that is solid or liquid at room temperature, such as hydrocarbon, fatty acid ester, aliphatic ketone, and aliphatic ether, if necessary.
炭化水素は、ポリエチレンワックス、フィッシャー・トロプシュワックス、パラフィンワックス等であってよく、例えば白油(Weissoel)と呼ばれる市販のパラフィン混合物であってよい。 The hydrocarbon may be polyethylene wax, Fischer-Tropsch wax, paraffin wax, and the like, for example, a commercially available paraffin mixture called white oil.
脂肪酸エステルは、炭素数1〜30の1〜6価アルコールと炭素数12〜30のカルボン酸との脂肪酸エステルであってよい。エステルに用いられる脂肪酸は、例えばラウリン酸、ミリスチン酸、パルミチン酸、ステアリン酸、オレイン酸、アラキン酸及びベヘニン酸等であってよく、好ましくはパルミチン酸、オレイン酸又はステアリン酸である。カルボン酸をエステル化するための炭素数1〜30の1価のアルコールとしては、例えばメタノール、エタノール、プロパノール、ブタノール、ヘキサノール、オクタノール、デカノール等、及び高級アルコールが挙げられる。2価アルコールとしては、例えばエチレングリコール、プロピレングリコール、ジエチレングリコール、トリエチレングリコール、シクロヘキサンジオール、ブタンジオール、ペンタンジオール、ヘキサンジオール、トリメチレングリコール、カテコール、レゾルシン、ハイドロキノン等が挙げられる。3価アルコールとしては、例えばグリセリン、トリメチロールプロパン、トリメチロールエタン、ブタントリオール、ペンタントリオール等が挙げられる。4価アルコールとしては、例えばペンタエリスリトール、ジグリセリン、ソルビタン、マンニタン等が挙げられる。5価アルコールとしてはアラビット等が挙げられ、6価アルコールとしてはテトラグリセリン、ソルビット、マンニット等が挙げられる。また、脂肪酸エステルは、牛脂、豚油、イワシ油、鯨油などの動物油脂、大豆油、トウモロコシ油、ヤシ油、アマニ油、ナタネ油、綿実油、ヒマシ油、キリ油などの植物油脂等の天然油脂、これらに水素添加して硬化処理を施した硬化油であってもよい。 The fatty acid ester may be a fatty acid ester of a 1 to 6 carbon alcohol having 1 to 30 carbon atoms and a carboxylic acid having 12 to 30 carbon atoms. The fatty acid used in the ester may be, for example, lauric acid, myristic acid, palmitic acid, stearic acid, oleic acid, arachidic acid, behenic acid, etc., preferably palmitic acid, oleic acid or stearic acid. Examples of the monovalent alcohol having 1 to 30 carbon atoms for esterifying the carboxylic acid include methanol, ethanol, propanol, butanol, hexanol, octanol, decanol, and higher alcohol. Examples of the dihydric alcohol include ethylene glycol, propylene glycol, diethylene glycol, triethylene glycol, cyclohexanediol, butanediol, pentanediol, hexanediol, trimethylene glycol, catechol, resorcin, and hydroquinone. Examples of the trihydric alcohol include glycerin, trimethylolpropane, trimethylolethane, butanetriol, pentanetriol and the like. Examples of the tetrahydric alcohol include pentaerythritol, diglycerin, sorbitan, mannitan and the like. Examples of the pentahydric alcohol include arabit, and examples of the hexavalent alcohol include tetraglycerin, sorbit, and mannitol. Fatty acid esters include animal fats such as beef tallow, pork oil, sardine oil, and whale oil, and natural fats such as vegetable oil such as soybean oil, corn oil, coconut oil, linseed oil, rapeseed oil, cottonseed oil, castor oil, and gill oil. Further, it may be a hardened oil obtained by hydrogenating them and subjected to a hardening treatment.
脂肪族ケトンは、16−ヘントリアコンタノン(パルミトン)、18−ペンタトリアコンタノン(ステアロン)、20−ノナトリアコンタノン(アラキノン)、及び22−トリアテトラコンタノン(ベヘノン)等の高級脂肪酸ケトンであってよい。 Aliphatic ketones are higher fatty acid ketones such as 16-hentriacontanone (palmitone), 18-pentatriacontanone (stearon), 20-nonatriacontanone (araquinone), and 22-triatetracontanone (behenone). It may be.
脂肪族エーテルは、チーグラー合成する際に副生する炭素数20〜40のアルキルエーテルであってよい。 The aliphatic ether may be an alkyl ether having 20 to 40 carbon atoms that is by-produced during Ziegler synthesis.
本発明に係る消泡剤は、貯蔵時の製品分離および増粘を防止するために、水溶性高分子を更に含んでもよい。水溶性高分子としては、セルロース、プルラン、アルギン酸ナトリウム、アラビアガム、グアーガム、グルコマンナン、キサンタンガム、ウェランガム、ラムザンガム、トラガントガム、ローカストビーンガム、アガロース、グリコーゲン、メチルセルロース、エチルセルロース、カルボキシメチルセルロース、ヒドロキシエチルセルロース、ヒドロキシプロピルセルロース、ヒドロキシプロピルメチルセルロース、ヒドロキシエチルメチルセルロース、カルボキシメチルエチルセルロース、酢酸フタル酸セルロース、ポリビニルアルコール、ポリエチレンオキサイド、ポリアクリルアミド、ポリメタクリルアミド、ポリアクリル酸、ポリメタクリル酸、アクリルアミドおよびアクリル酸の共重合物、アクリルアミド及びメタクリル酸の共重合物、メタクリルアミドおよびアクリルアミドの共重合物、メタクリルアミド及びメタクリル酸の共重合物等が挙げられる。 The antifoaming agent according to the present invention may further contain a water-soluble polymer in order to prevent product separation and thickening during storage. Water-soluble polymers include cellulose, pullulan, sodium alginate, gum arabic, guar gum, glucomannan, xanthan gum, welan gum, rhamzan gum, tragacanth gum, locust bean gum, agarose, glycogen, methylcellulose, ethylcellulose, carboxymethylcellulose, hydroxyethylcellulose, hydroxypropyl Cellulose, hydroxypropylmethylcellulose, hydroxyethylmethylcellulose, carboxymethylethylcellulose, cellulose acetate phthalate, polyvinyl alcohol, polyethylene oxide, polyacrylamide, polymethacrylamide, polyacrylic acid, polymethacrylic acid, copolymer of acrylamide and acrylic acid, acrylamide And methacrylic acid Things, a copolymer of methacrylamide and acrylamide, a copolymer such as of methacrylamide and methacrylic acid.
その他、本発明に係る消泡剤は、更に、防腐剤、防かび剤、殺菌剤、防錆剤、皮張り防止剤等を含んでもよい。これらはいずれも従来周知である(例えば特開2000−300909号公報参照)ため、その詳細は省略する。 In addition, the antifoaming agent according to the present invention may further contain a preservative, a fungicide, a bactericidal agent, a rust inhibitor, a skin prevention agent, and the like. Since these are conventionally well-known (see, for example, Japanese Patent Laid-Open No. 2000-300909), details thereof are omitted.
本発明に係る消泡剤は、以上の成分を含む油相が、水相中に乳化されて分散されたものである。油相と水相との混合比率は、O/Wエマルション構造が得られる限りにおいて特に限定されず、一般的には油相の量が消泡剤に対し50質量%以下であればよい。 The antifoaming agent according to the present invention is an oil phase containing the above components emulsified and dispersed in an aqueous phase. The mixing ratio of the oil phase and the aqueous phase is not particularly limited as long as an O / W emulsion structure is obtained, and generally the amount of the oil phase may be 50% by mass or less based on the antifoaming agent.
本発明に係る消泡剤は、高級アルコールとマイクロクリスタリンワックス及び/又はペトロラタムとを含む液状の油剤を、多価アルコールの存在下で、水へと乳化させてO/Wエマルションを生成する乳化工程を有する。これにより、乳化後の冷却過程における油相の凝集が抑制され、消泡効果に優れる消泡剤を得ることができる。 The antifoaming agent according to the present invention is an emulsification step in which a liquid oil containing a higher alcohol and microcrystalline wax and / or petrolatum is emulsified in water in the presence of a polyhydric alcohol to produce an O / W emulsion. Have Thereby, aggregation of the oil phase in the cooling process after emulsification is suppressed, and an antifoaming agent having an excellent defoaming effect can be obtained.
乳化工程において、多価アルコールは、油相の凝集をより十分に抑制する観点で、高級アルコールとマイクロクリスタリンワックス及び/又はペトロラタム等の油剤と混合した後に水へ添加することが好ましいが、油剤とは別に水へと添加されてもよい。 In the emulsification step, the polyhydric alcohol is preferably added to water after being mixed with a higher alcohol and an oil agent such as microcrystalline wax and / or petrolatum from the viewpoint of sufficiently suppressing aggregation of the oil phase. Alternatively, it may be added to water.
前述のように、多価アルコールの配合量は、マイクロクリスタリンワックス及び/又はペトロラタムの合量100質量部に対し、10質量部以上200質量部以下であることが好ましく、油剤には他の成分を任意に含めてよい。 As described above, the blending amount of the polyhydric alcohol is preferably 10 parts by mass or more and 200 parts by mass or less with respect to 100 parts by mass of the total amount of the microcrystalline wax and / or petrolatum, and the oil agent contains other components. Optionally included.
乳化工程では、油剤を水へと分散させるため、油剤が流動性を有するよう、油剤に含まれる成分の融点以上の温度(特に限定されないが、90℃以上)へと加熱し、油剤及び水を撹拌する。その操作や設備自体は従来周知である(特開平11−276805号公報参照)ため、詳細は省略する。 In the emulsification step, in order to disperse the oil agent in water, the oil agent is heated to a temperature not lower than the melting point of the components contained in the oil agent (not particularly limited, but 90 ° C. or higher) so that the oil agent has fluidity. Stir. Since the operation and equipment itself are well known in the art (see Japanese Patent Application Laid-Open No. 11-276805), details are omitted.
乳化工程の後には、O/Wエマルションを常温へと冷却する工程を伴う。この工程は、乳化工程より穏やかな撹拌を行い、又は撹拌を行わず、O/Wエマルションを常温よりも高い所定温度まで冷却する第1冷却工程と、その後、第1冷却工程より激しい撹拌を行いながら、O/Wエマルションを常温へと冷却する第2冷却工程と、有することが好ましい。これにより、冷却過程における油相の凝集をより十分に抑制することができる。 The emulsification step is followed by a step of cooling the O / W emulsion to room temperature. In this step, the first cooling step in which the O / W emulsion is cooled to a predetermined temperature higher than normal temperature without stirring, and then the stirring is performed more intensely than in the first cooling step. However, it is preferable to have the 2nd cooling process which cools O / W emulsion to normal temperature. Thereby, aggregation of the oil phase in the cooling process can be more sufficiently suppressed.
所定温度は、油剤の組成、水との混合比率等に応じて、消泡剤の粒子表面が固化する温度となるよう適宜決定されてよく、一般的には30℃以上60℃以下であってよい。なお、撹拌が穏やか又は激しいとは、せん断力の大小(例えば、乳化工程、第1冷却工程、第2冷却工程が同じ設備で行われる場合、撹拌部材の回転速度の大小)によって決定される。 The predetermined temperature may be appropriately determined according to the composition of the oil agent, the mixing ratio with water, and the like so as to be a temperature at which the particle surface of the antifoaming agent is solidified. Good. Note that the gentle or intense stirring is determined by the magnitude of the shearing force (for example, when the emulsification step, the first cooling step, and the second cooling step are performed in the same equipment, the rotation speed of the stirring member).
ただし、冷却工程では、従来周知のように、O/Wエマルションの撹拌を続けながら常温へと冷却してもよい。 However, in the cooling step, as is conventionally known, the O / W emulsion may be cooled to room temperature while continuing to stir.
このようにして得られる消泡剤は、例えば、紙パルプ工業、食品工業、繊維工業、建材用ボード製造、塗料工業、化学工業等での加工工程及び排水処理工程において幅広く使用でき、特に抄紙工程や活性汚泥等の排水処理工程において有用である。 The antifoaming agent thus obtained can be widely used, for example, in the paper pulp industry, food industry, textile industry, building material board production, paint industry, chemical industry, etc. It is useful in wastewater treatment processes such as activated sludge.
<実施例1〜4、比較例1〜4>
表1に示す成分をジャケット式ビーカー内に供給し、循環式恒温水s槽「Ecoline」(LAUDA社製)に90℃の温水を通水することで加熱し、溶融させた。撹拌機「トオルネード(スタンダードタイプ)」(アズワン社製)を2000rpmで回転させ、溶融した油剤へと温水を撹拌しながら添加することで、油剤を水へと乳化させてO/Wエマルションを生成した。その後、撹拌を続けながら、O/Wエマルションに対し、アクリル酸系ポリマー「アクアリックDL40S」(日本触媒社製)を0.1質量%添加した。
<Examples 1-4, Comparative Examples 1-4>
The components shown in Table 1 were supplied into a jacket-type beaker, and heated and melted by passing hot water of 90 ° C. through a circulating constant temperature water s tank “Ecoline” (manufactured by LAUDA). The stirrer “Toornade (standard type)” (manufactured by ASONE) was rotated at 2000 rpm, and hot water was added to the molten oil while stirring to emulsify the oil into water to produce an O / W emulsion. . Then, 0.1 mass% of acrylic acid polymer “AQUALIC DL40S” (manufactured by Nippon Shokubai Co., Ltd.) was added to the O / W emulsion while continuing stirring.
撹拌を停止し、循環式恒温水槽へと通水する水を冷水に切換え、O/Wエマルションを60℃程度にまで冷却させた。その後、再び撹拌を開始し(回転速度500rpm)、撹拌しながらO/Wエマルションを常温(30℃以下)へと冷却することで、消泡剤を得た。 Stirring was stopped, the water passing through the circulation type thermostatic water tank was switched to cold water, and the O / W emulsion was cooled to about 60 ° C. Then, stirring was started again (rotation speed 500rpm), and the O / W emulsion was cooled to normal temperature (30 degrees C or less), stirring, and the antifoamer was obtained.
[評価]
得られた各々の消泡剤を4mg/Lの量で添加した新聞用紙の抄紙白水500mLを、内径70mm、容量1Lの目盛付きガラス製円筒容器に供給し、循環ポンプにより1000mL/分の流量で循環させ、円筒容器内の抄紙白水の水面上50cmの高さから、水面へと落下させた。温度を45℃に維持し、循環開始5分後において、円筒容器内の抄紙白水の水面上に生じた泡の厚みを、目盛りに基づき読み取った。この結果を表1に示す。
[Evaluation]
500 mL of newsprint paper white water to which each of the obtained antifoams was added in an amount of 4 mg / L was supplied to a glass cylindrical container with a caliber of 70 mm in inner diameter and 1 L in capacity, and at a flow rate of 1000 mL / min by a circulation pump. It was circulated and dropped onto the water surface from a height of 50 cm above the surface of the papermaking white water in the cylindrical container. The temperature was maintained at 45 ° C., and 5 minutes after the start of circulation, the thickness of the foam generated on the surface of the papermaking white water in the cylindrical container was read based on the scale. The results are shown in Table 1.
マイクロクリスタリンワックス Hi−mic−1090(日本精蝋社製)
高級アルコール NAFOL20+(サソールジャパン社製)
炭化水素 パラフィンワックス155(日本精蝋社製)
脂肪酸エステル ヒマシ硬化油(伊藤製油社製)
多価アルコール プロピレングリコール試薬1級(キシダ化学社製)
Microcrystalline wax Hi-mic-1090 (Nippon Seiwa Co., Ltd.)
Higher alcohol NAFOL20 + (manufactured by Sasol Japan)
Hydrocarbon paraffin wax 155 (Nippon Seiwa Co., Ltd.)
Fatty acid ester castor hydrogenated oil (Ito Oil Co., Ltd.)
Polyhydric alcohol Propylene glycol reagent grade 1 (Kishida Chemical Co., Ltd.)
表1に示されるように、実施例1〜4は、比較例1〜4に比べ発泡量が小さく、消泡効果に優れることが分かった。また、実施例1及び2より、優れる消泡効果を得るためには、マイクロクリスタリンワックス、高級アルコール及び多価アルコールが必須である一方、炭化水素及び脂肪酸エステルは必ずしも必要でないことも確認された。 As shown in Table 1, it was found that Examples 1 to 4 had a smaller foaming amount than Comparative Examples 1 to 4 and were excellent in the defoaming effect. Further, from Examples 1 and 2, it was confirmed that in order to obtain an excellent defoaming effect, microcrystalline wax, higher alcohol and polyhydric alcohol are essential, but hydrocarbon and fatty acid ester are not necessarily required.
<実施例5〜13、比較例5〜13>
多価アルコールの種類を表2に示すものにした点を除き、実施例1と同様の手順で消泡剤を得た。得た消泡剤について、100メッシュの金網でろ過し、ろ過残渣の量を測定することで、油相の凝集の有無を確認した。この結果を表2に示す。
<Examples 5 to 13 and Comparative Examples 5 to 13>
An antifoaming agent was obtained in the same procedure as in Example 1 except that the type of polyhydric alcohol was changed to that shown in Table 2. About the obtained antifoamer, it filtered with the 100 mesh metal-mesh, and the presence or absence of aggregation of an oil phase was confirmed by measuring the quantity of the filtration residue. The results are shown in Table 2.
表2において、実施例5〜13における凝集無しは残渣の量が油剤の配合量に対し0.1%未満であり、比較例5〜13における凝集有りは残渣の量が油剤の配合量に対し5%以上であった。これにより、マイクロクリスタリンワックス及び高級アルコールとともに、あらゆる多価アルコールを併用して、油相の凝集を抑制できることが分かった。 In Table 2, without aggregation in Examples 5 to 13, the amount of the residue is less than 0.1% with respect to the blending amount of the oil agent, and with aggregation in Comparative Examples 5 to 13 the amount of the residue with respect to the blending amount of the oil agent It was 5% or more. Thereby, it turned out that aggregation of an oil phase can be suppressed by using all polyhydric alcohols together with microcrystalline wax and higher alcohol.
Claims (3)
前記乳化工程より穏やかな撹拌を行い、又は撹拌を行わず、前記O/Wエマルションを常温よりも高い所定温度まで冷却する第1冷却工程と、
その後、第1冷却工程より激しい撹拌を行いながら、前記O/Wエマルションを常温へと冷却する第2冷却工程と、を更に有する請求項2記載の製造方法。 After the emulsification step,
A first cooling step in which the O / W emulsion is cooled to a predetermined temperature higher than room temperature without gentle stirring or stirring than the emulsification step;
Then, the manufacturing method of Claim 2 which further has a 2nd cooling process which cools the said O / W emulsion to normal temperature, stirring more intensely than a 1st cooling process.
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