[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

JP4478423B2 - Method for producing granulated titanium dioxide pigment - Google Patents

Method for producing granulated titanium dioxide pigment Download PDF

Info

Publication number
JP4478423B2
JP4478423B2 JP2003336074A JP2003336074A JP4478423B2 JP 4478423 B2 JP4478423 B2 JP 4478423B2 JP 2003336074 A JP2003336074 A JP 2003336074A JP 2003336074 A JP2003336074 A JP 2003336074A JP 4478423 B2 JP4478423 B2 JP 4478423B2
Authority
JP
Japan
Prior art keywords
titanium dioxide
dioxide pigment
granulated
pressure
granulation
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.)
Expired - Fee Related
Application number
JP2003336074A
Other languages
Japanese (ja)
Other versions
JP2005104997A (en
Inventor
英雄 高橋
薫 磯部
和紀 小原田
浩樹 加藤
佳治 津郷
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ishihara Sangyo Kaisha Ltd
Original Assignee
Ishihara Sangyo Kaisha Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ishihara Sangyo Kaisha Ltd filed Critical Ishihara Sangyo Kaisha Ltd
Priority to JP2003336074A priority Critical patent/JP4478423B2/en
Publication of JP2005104997A publication Critical patent/JP2005104997A/en
Application granted granted Critical
Publication of JP4478423B2 publication Critical patent/JP4478423B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Pigments, Carbon Blacks, Or Wood Stains (AREA)
  • Inorganic Compounds Of Heavy Metals (AREA)

Description

本発明は造粒二酸化チタン顔料及びその製造方法に関する。   The present invention relates to a granulated titanium dioxide pigment and a method for producing the same.

二酸化チタンは可視光の屈折率が高く、白色度、隠ペイ性に優れており、白色顔料として塗料、インキ、プラスチックス、紙等の各種組成物に配合されて広く用いられている。しかし、二酸化チタン顔料粉末は流動性があまり良好ではない。例えば、保管中や前記の各種組成物の製造工程での輸送・移送、フィード、予備混合、包装等の操作の際に、機器の内部で流動不良を生じたり、流動不良により堆積した二酸化チタン顔料粉末が機器内壁に強く付着して機器に閉塞を生じさせる等、生産性を著しく低下させることがある。また、一部の二酸化チタン顔料粉末は発塵性が大きく、作業環境にも影響を与えている。   Titanium dioxide has a high refractive index of visible light, is excellent in whiteness and hiding property, and is widely used as a white pigment by blending it into various compositions such as paints, inks, plastics and paper. However, the titanium dioxide pigment powder is not very good in fluidity. For example, titanium dioxide pigments that cause flow defects inside the equipment or are deposited due to flow defects during operations such as transportation, transfer, feed, premixing, packaging, etc. during storage or in the manufacturing process of the various compositions described above. Productivity may be significantly reduced, for example, the powder may adhere strongly to the inner wall of the device and cause the device to become clogged. In addition, some titanium dioxide pigment powders have a high dusting property and affect the working environment.

粉末の流動性及び作業性を改善する方法として、粉末を造粒する技術が提案されている。一般的に粉末の造粒には加圧成形、攪拌成形、押出し成形、転動成形、流動層成形、噴霧乾燥等の機械的な手法が用いられており、ベントナイト、タルク等の粘土鉱物、水、アルコール等の溶媒、ポリビニルアルコール等の高分子化合物等を、成形の際にバインダーとして加えて造粒物の強度を高めている(非特許文献1参照)。また、二酸化チタン等の顔料粉末については、高級脂肪酸またはその金属塩等の分散剤をバインダーとして用いて造粒する方法が知られている(特許文献1参照)。   As a method for improving the fluidity and workability of the powder, a technique for granulating the powder has been proposed. In general, mechanical methods such as pressure molding, stirring molding, extrusion molding, rolling molding, fluidized bed molding, spray drying, etc. are used for granulating powder, clay minerals such as bentonite and talc, water In addition, a solvent such as alcohol or a polymer compound such as polyvinyl alcohol is added as a binder during molding to increase the strength of the granulated product (see Non-Patent Document 1). In addition, a pigment powder such as titanium dioxide is known to be granulated using a dispersant such as a higher fatty acid or a metal salt thereof as a binder (see Patent Document 1).

「造粒ハンドブック」、初版、オーム社刊、1991年3月10日、p.11、203−204“Granulation Handbook”, first edition, published by Ohmsha, March 10, 1991, p. 11, 203-204 特公昭54−7287号公報(第1〜3頁)Japanese Patent Publication No.54-7287 (pages 1 to 3)

前記非特許文献1に記載の方法を二酸化チタン顔料粉末に適用する場合、例えば溶媒をバインダーに用いると、溶媒が蒸発する際に二酸化チタン顔料粉末が強固に凝集するため、分散性の低下を来した。そのため、二酸化チタン顔料を一次粒子にまでに再分散させるのに過大なエネルギーを必要とした。また、粘土鉱物や高分子化合物をバインダーとして用いると、適度な硬度を有する造粒物に調整することはできても、白色度、隠ペイ性等の光学特性の低下を来した。一方、前記特許文献1に記載の方法では、分散剤がバインダーとしても作用するので、流動性及び作業性と分散性とのバランスが取れた造粒物が得られるが、上記各種組成物に配合される酸化チタン以外の成分(樹脂成分や添加剤)に適した分散剤を選択する必要があり、適用範囲が大きく限定された。本発明では以上に述べた従来技術の課題を克服し、流動性、作業性に優れ、造粒による分散性の差がほとんど生じない、しかも汎用性の高い造粒二酸化チタン顔料及びその製造方法を提供するものである。   When the method described in Non-Patent Document 1 is applied to titanium dioxide pigment powder, for example, when a solvent is used as a binder, the titanium dioxide pigment powder aggregates strongly when the solvent evaporates, resulting in a decrease in dispersibility. did. Therefore, excessive energy was required to redisperse the titanium dioxide pigment to the primary particles. In addition, when clay minerals or polymer compounds are used as binders, optical properties such as whiteness and hiding property are deteriorated even though they can be adjusted to a granulated product having an appropriate hardness. On the other hand, in the method described in Patent Document 1, since the dispersant also acts as a binder, a granulated product having a balance between fluidity and workability and dispersibility can be obtained. It is necessary to select a dispersant suitable for components (resin components and additives) other than titanium oxide, and the application range is greatly limited. The present invention overcomes the above-described problems of the prior art, has excellent fluidity and workability, hardly causes a difference in dispersibility due to granulation, and has a highly versatile granulated titanium dioxide pigment and a method for producing the same. It is to provide.

本発明者らはこれらの課題を解決すべく鋭意研究を重ねた結果、バインダーを用いなくても、二酸化チタン顔料の分散性を損なわない造粒二酸化チタン顔料及びその製造方法を見出し、本発明を完成させた。   As a result of intensive studies to solve these problems, the present inventors have found a granulated titanium dioxide pigment that does not impair the dispersibility of the titanium dioxide pigment without using a binder, and a method for producing the same, and Completed.

すなわち、本発明は、二酸化チタン顔料粉末をバインダーを含まないで造粒してなり、分散度が低くとも−1.5であることを特徴とする造粒二酸化チタン顔料である。さらに本発明は、二酸化チタン顔料粉末をバインダーを用いずに0.1〜10MPaの範囲の圧力で加圧造粒することを特徴とする造粒二酸化チタン顔料の製造方法である。   That is, the present invention is a granulated titanium dioxide pigment obtained by granulating a titanium dioxide pigment powder without containing a binder and having a dispersity of at least -1.5. Furthermore, this invention is a manufacturing method of the granulated titanium dioxide pigment characterized by carrying out the pressure granulation of the titanium dioxide pigment powder by the pressure of the range of 0.1-10 Mpa, without using a binder.

本発明の造粒二酸化チタン顔料を塗料、インキ、プラスチックス、紙等の各種組成物に配合して用いると、(1)輸送・包装時のハンドリング性や計量精度が改善でき、付着による二酸化チタン顔料の損失を低減できる等、優れた流動性を有し、(2)粉塵の発生が抑制され作業環境を改善できる等、優れた作業性を有し、(3)粉末と同等の分散性を有し、しかも(4)バインダーを用いていないので汎用性が高いものである。   When the granulated titanium dioxide pigment of the present invention is blended and used in various compositions such as paints, inks, plastics, paper, etc., (1) handling properties and measuring accuracy during transportation and packaging can be improved, and titanium dioxide due to adhesion Excellent fluidity, such as reduced pigment loss, (2) Excellent workability, such as reduced dust generation and improved working environment, (3) Dispersibility equivalent to powder And (4) versatility because no binder is used.

本発明は造粒二酸化チタン顔料であって、二酸化チタン顔料粉末をバインダーを含まないで造粒してなり、分散度が低くとも−1.5であることを特徴とする。本発明の造粒二酸化チタン顔料は、流動性、作業性に優れ、しかもバインダーを用いずに造粒されているので汎用性が高く、広範囲の組成物に適用できる。本発明におけるバインダーとは、造粒時に二酸化チタン粒子を結着させる作用を有するものを言い、例えば、ベントナイト、タルク等の粘土鉱物、水、アルコール等の溶媒、ポリビニルアルコール等の高分子化合物、高級脂肪酸またはその金属塩等の分散剤が挙げられる。   The present invention is a granulated titanium dioxide pigment, characterized by granulating titanium dioxide pigment powder without containing a binder, and having a dispersity of at least -1.5. The granulated titanium dioxide pigment of the present invention is excellent in fluidity and workability, and is granulated without using a binder, so that it has high versatility and can be applied to a wide range of compositions. The binder in the present invention refers to one having an action of binding titanium dioxide particles during granulation, for example, clay minerals such as bentonite and talc, water, solvents such as alcohol, polymer compounds such as polyvinyl alcohol, and the like Examples thereof include dispersants such as fatty acids or metal salts thereof.

本発明における「分散度」は下記の方法で評価したものである。   The “dispersion degree” in the present invention is evaluated by the following method.

(分散度の評価方法)
気流式粉砕機(200AF型:富士産業社製)を用い、粉砕媒に加圧空気を用いて、造粒二酸化チタン顔料500gを200g/分の速度で粉砕機に添加して造粒物を粉砕し、元の一次粒子にまで再分散させる。すなわち、造粒前の二酸化チタン顔料粉末の状態に戻す操作を施す。下記の表1に示す処方1にて粉砕前後の試料を各々、容量130ccのガラス製容器に仕込み、ペイントコンディショナー(レッドデビル社製)を用いて20分間分散して分散液を調整した後、下記の表2に示す処方2にて、樹脂成分1重量部に対し二酸化チタン顔料1重量部、固形分体積濃度46%の塗料とする。これら粉砕前後の試料を用いて作成した塗料を、それぞれ4ミルアプリケーターでガラス板に塗布し、30分間静置してから、120℃の温度で30分間焼き付け塗膜化する。得られた塗膜の20°光沢度をグロスメーター(GM−26D型/村上色材研究所製)を用いて計測する。(粉砕前の20°光沢度)−(粉砕後の20°光沢度)を算出し、これを「分散度」とする。
(Dispersion evaluation method)
Using an air-flow type pulverizer (200AF type: manufactured by Fuji Sangyo Co., Ltd.), using compressed air as a pulverizing medium, 500g of granulated titanium dioxide pigment is added to the pulverizer at a rate of 200g / min to pulverize the granulated product. And redispersed to the original primary particles. That is, an operation of returning to the state of the titanium dioxide pigment powder before granulation is performed. Each of the samples before and after pulverization in Formula 1 shown in Table 1 below was placed in a 130 cc glass container and dispersed for 20 minutes using a paint conditioner (manufactured by Red Devil). In Table 2 shown in Table 2, the coating composition is 1 part by weight of titanium dioxide pigment and 46% solids volume concentration with respect to 1 part by weight of the resin component. The paints prepared using the samples before and after pulverization are each applied to a glass plate with a 4 mil applicator and allowed to stand for 30 minutes, and then baked at 120 ° C. for 30 minutes to form a coating film. The 20 ° glossiness of the obtained coating film is measured using a gloss meter (GM-26D type / Murakami Color Materials Laboratory). (20 ° gloss before pulverization) − (20 ° gloss after pulverization) is calculated, and this is defined as “dispersion”.

本発明ではこの分散度が低くとも−1.5である。即ち、造粒前の二酸化チタン顔料粉末が有する優れた分散性を造粒後も保持している。尚、分散度には特に上限は無いが、本発明においては、通常、粉砕前後で20°光沢度には有意差が無いので、上限は+2.0未満となる。従って、本発明の造粒二酸化チタン顔料は、塗料、インキ、プラスチックス、紙等の組成物の製造において工業的に常用される分散機によって剪断力を加えれば、造粒物を一次粒子にまで容易に分散させることができる。   In the present invention, this dispersity is at least -1.5. That is, the excellent dispersibility of the titanium dioxide pigment powder before granulation is retained after granulation. Although there is no particular upper limit for the degree of dispersion, in the present invention, there is usually no significant difference in the 20 ° gloss before and after pulverization, so the upper limit is less than +2.0. Therefore, the granulated titanium dioxide pigment of the present invention can be made into a primary particle by applying a shearing force by a dispersing machine commonly used in industry in the production of compositions such as paints, inks, plastics and paper. It can be easily dispersed.

Figure 0004478423
Figure 0004478423

Figure 0004478423
Figure 0004478423

また、本発明では、硬度が1〜20gの範囲にあることを特徴とする造粒二酸化チタン顔料である。本発明の造粒二酸化チタン顔料は、前記範囲の硬度を有するので、輸送、移送、保管等の途中では造粒物がほとんど壊れることがない。なお、本発明において硬度は下記方法で算出した値である。   In the present invention, the granulated titanium dioxide pigment has a hardness in the range of 1 to 20 g. Since the granulated titanium dioxide pigment of the present invention has a hardness in the above range, the granulated product is hardly broken during transportation, transfer, storage and the like. In the present invention, the hardness is a value calculated by the following method.

(硬度の測定方法)
電子天秤の上に造粒二酸化チタン顔料を一つ置き、このものを上からスパチュラで圧縮し、破砕した時の天秤の指示値を読み取る。この操作を一試料につき少なくとも20回繰り返して、それら指示値の平均値を算出し、造粒二酸化チタン顔料の硬度とする。
(Measurement method of hardness)
Place one granulated titanium dioxide pigment on the electronic balance, compress this with a spatula from the top, and read the indicated value of the balance when crushed. This operation is repeated at least 20 times per sample, and the average value of the indicated values is calculated to obtain the hardness of the granulated titanium dioxide pigment.

なお、流動性及び作業性を評価する物性値としては、安息角及び嵩密度を夫々用いた。安息角は、24メッシュの篩を通した試料を、漏斗を用いて80mmφの円形テーブル上に山状に注ぎ、試料の山とテーブルと接地角を3箇所で計測し、それらの平均値を用いる。安息角が小さい粉体程、流動性に優れている。本発明の造粒二酸化チタン顔料の安息角は最大でも45°と小さく、二酸化チタン顔料粉末と比べて良好な流動性を示す。また、二酸化チタン顔料粉末は粒子が小さいので、製造過程で空気を巻き込み易く、流動性以外にも嵩密度が大きく取り扱い難いという作業性に問題もあった。本発明の造粒二酸化チタン顔料は、嵩密度を0.8g/cc以上に高くすることができ、二酸化チタン顔料粉末と比べて作業性が更に向上する。なお、嵩密度はJIS K5101に基づいて測定する。   In addition, the angle of repose and the bulk density were used as physical property values for evaluating fluidity and workability. For the angle of repose, a sample passed through a 24-mesh sieve was poured in a mountain shape on a circular table of 80 mmφ using a funnel, the sample crest, table and ground contact angle were measured at three locations, and the average value was used. . The smaller the angle of repose, the better the fluidity. The angle of repose of the granulated titanium dioxide pigment of the present invention is as small as 45 ° at the maximum, and shows good fluidity compared with the titanium dioxide pigment powder. In addition, since the titanium dioxide pigment powder has small particles, air is easily involved in the manufacturing process, and there is a problem in workability that the bulk density is large and difficult to handle in addition to fluidity. The granulated titanium dioxide pigment of the present invention can increase the bulk density to 0.8 g / cc or more, and the workability is further improved as compared with the titanium dioxide pigment powder. The bulk density is measured based on JIS K5101.

本発明の造粒二酸化チタン顔料の形状はフレーク状、顆粒状、粒塊状、不定形等特に制限は無く、本発明の効果を損なわない範囲で未造粒の二酸化チタン顔料粉末が含まれていても良い。造粒物の大きさは特に限定されず、流動性、作業性等の所望の効果が得られる範囲で、後述の造粒条件や、分級、壊砕・整粒等の操作により適宜設定することができる。   The shape of the granulated titanium dioxide pigment of the present invention is not particularly limited, such as flakes, granules, agglomerates, and irregular shapes, and includes ungranulated titanium dioxide pigment powder as long as the effects of the present invention are not impaired. Also good. The size of the granulated product is not particularly limited, and may be set as appropriate by the granulation conditions described later, and operations such as classification, crushing and sizing within a range where desired effects such as fluidity and workability can be obtained. Can do.

造粒に用いる二酸化チタン顔料粉末としては、平均粒子径(電子顕微鏡法による一次粒子の50%粒子径)が0.1〜0.5μmの範囲の範囲にあるものが、隠ペイ性が高いので好ましく、より好ましい範囲は0.1〜0.4μmである。その結晶形はルチル型、アナターゼ型のいずれでも良く、またそれらの混合物でも、部分的に非晶質の二酸化チタンが含まれていても良い。また、上記二酸化チタン顔料粉末は、例えば、硫酸チタン溶液を加水分解する所謂硫酸法によって得られるものでも、ハロゲン化チタンを気相酸化する所謂塩素法によって得られるものであっても良く、製造方法は特に限定されない。   As the titanium dioxide pigment powder used for granulation, those having an average particle diameter (50% particle diameter of primary particles by electron microscopy) in the range of 0.1 to 0.5 μm have high concealment properties. A more preferable range is 0.1 to 0.4 μm. The crystal form may be either a rutile type or an anatase type, or a mixture thereof or partially containing amorphous titanium dioxide. The titanium dioxide pigment powder may be obtained by, for example, a so-called sulfuric acid method for hydrolyzing a titanium sulfate solution, or may be obtained by a so-called chlorine method for vapor-phase oxidation of titanium halide. Is not particularly limited.

一般的に、無機化合物で表面が被覆された二酸化チタン顔料は耐候性・耐光性が、有機化合物の被覆では樹脂成分との親和性が更に改良される。このため、本発明において二酸化チタン顔料粉末としては、予めこれらの少なくとも1種で表面が被覆されたものが好ましい。無機化合物の被覆量は、用途によって異なるが、塗料やインキ組成物に用いる場合は0.1〜10重量%、プラスチックス組成物の場合は0.05〜5重量%の範囲が好ましい。有機化合物の好ましい被覆量は通常0.01〜5重量%の範囲であり、更に好ましい範囲は0.05〜2重量%である。   In general, a titanium dioxide pigment whose surface is coated with an inorganic compound is further improved in weather resistance and light resistance, and an organic compound coating is further improved in affinity with a resin component. For this reason, the titanium dioxide pigment powder in the present invention is preferably one whose surface is previously coated with at least one of these. The coating amount of the inorganic compound varies depending on the application, but it is preferably in the range of 0.1 to 10% by weight when used in paints and ink compositions, and 0.05 to 5% by weight in the case of plastics compositions. A preferable coating amount of the organic compound is usually in the range of 0.01 to 5% by weight, and a more preferable range is 0.05 to 2% by weight.

本発明で二酸化チタン顔料粉末の表面被覆に用いる無機化合物としては、アルミニウム、ケイ素、ジルコニウム、スズ、チタニウム、アンチモン等の酸化物、水酸化物、水和酸化物、あるいはリン酸塩等が挙げられ、中でも、アルミニウム、ケイ素、ジルコニウム、スズの化合物が好ましい。これらは1種が被覆されていても、2種以上の被覆が積層されたり、2種以上の無機化合物の混合物が被覆されても良く、また、多孔層として被覆されても、緻密層であっても良く、特に制限されない。   Examples of the inorganic compound used for the surface coating of the titanium dioxide pigment powder in the present invention include oxides such as aluminum, silicon, zirconium, tin, titanium, and antimony, hydroxides, hydrated oxides, and phosphates. Of these, compounds of aluminum, silicon, zirconium and tin are preferred. These may be a single layer, a laminate of two or more types of coatings, a mixture of two or more types of inorganic compounds, and a dense layer even when coated as a porous layer. There is no particular limitation.

本発明で二酸化チタン顔料粉末の表面被覆に用いる有機化合物としては、多価アルコール、アルカノールアミンまたはその誘導体、有機ケイ素化合物、高級脂肪属炭化水素等を用いることができ、中でも、多価アルコール、アルカノールアミン、有機ケイ素化合物が好ましい。具体的には、例えば、多価アルコールとしてはトリメチロールエタン、トリメチロールプロパン、ペンタエリスリトール等が、アルカノールアミンとしてはトリエチルアミン、トリメチルアミン等が、有機ケイ素化合物としてはジメチルポリシロキサン、メチルハイドロジェンポリシロキサン等のポリシロキサン類、アミノシラン、ビニルシラン等のシランカップリング剤、アルキルシラン類、フェニルシラン類、フルオロアルキルシラン類等が、高級脂肪属炭化水素としてはパラフィンワックス、ポリエチレンワックス等が挙げられ、これらが1種被覆されたものであっても、2種以上がを組合せて被覆されたものであっても良い。   As the organic compound used for the surface coating of the titanium dioxide pigment powder in the present invention, polyhydric alcohol, alkanolamine or a derivative thereof, organosilicon compound, higher aliphatic hydrocarbon, etc. can be used, among which polyhydric alcohol, alkanol. Amines and organosilicon compounds are preferred. Specifically, for example, trimethylolethane, trimethylolpropane, pentaerythritol, etc. as polyhydric alcohol, triethylamine, trimethylamine, etc. as alkanolamine, dimethylpolysiloxane, methylhydrogenpolysiloxane, etc. as organosilicon compounds Polysiloxanes, silane coupling agents such as amino silane and vinyl silane, alkyl silanes, phenyl silanes, fluoroalkyl silanes and the like, and higher aliphatic hydrocarbons include paraffin wax, polyethylene wax and the like. Even what was seed-coated may be coated with a combination of two or more.

次に、本発明は造粒二酸化チタン顔料の製造方法であって、二酸化チタン顔料粉末をバインダーを用いずに0.1〜10MPaの範囲の圧力で加圧造粒することを特徴とする。本発明の製造方法では、二酸化チタン顔料粉末を前記範囲の圧力で加圧造粒することで、バインダーを用いなくとも、造粒による分散性の低下がほとんどなく、しかも流動性及び作業性に優れた造粒二酸化チタン顔料が得られる。圧力が前記範囲より低いと十分な流動性及び作業性が得られず、高いと分散性が低下してしまう。より好ましい圧力の範囲は、0.1〜5MPaである。   Next, this invention is a manufacturing method of a granulated titanium dioxide pigment, Comprising: It pressurizes and granulates the titanium dioxide pigment powder by the pressure of the range of 0.1-10 Mpa, without using a binder. In the production method of the present invention, by subjecting the titanium dioxide pigment powder to pressure granulation at a pressure in the above range, there is almost no decrease in dispersibility due to granulation and excellent fluidity and workability without using a binder. A granulated titanium dioxide pigment is obtained. When the pressure is lower than the above range, sufficient fluidity and workability cannot be obtained, and when the pressure is higher, the dispersibility is lowered. A more preferable pressure range is 0.1 to 5 MPa.

加圧造粒には、ロール成形機、プレス成形機、打錠成形機等の公知の加圧成形機を用いることができ、中でもロール成形機は多量の二酸化チタン顔料粉末を連続造粒できるので工業的に好ましい。造粒時の圧力を前記範囲に制御するには、ロール成形機を用いる場合、ロールのクリアランス、回転数、二酸化チタン顔料粉末の供給量等を調整したり、ロール面の材質を金属、プラスチックス、ゴム等から適宜選択することで行う。ロール成形機としては、例えば、開放式ロール、ブリケッティングロール等が挙げられ、ロール表面は平滑であっても波型であっても良く、凹状のポケットや凸状のブリケットが設けられていてもよく、特に制限は無い。ロール数やロール径は生産量に応じて適宜選択できるが、ロール数は2本のものが一般的である。   For pressure granulation, a known pressure molding machine such as a roll molding machine, a press molding machine, a tableting molding machine or the like can be used, and among them, the roll molding machine can continuously granulate a large amount of titanium dioxide pigment powder. Industrially preferable. In order to control the pressure at the time of granulation within the above range, when using a roll forming machine, the clearance of the roll, the number of rotations, the supply amount of titanium dioxide pigment powder, etc. are adjusted, or the roll surface material is made of metal, , By appropriately selecting from rubber or the like. Examples of the roll forming machine include an open roll and a briquetting roll. The roll surface may be smooth or corrugated and provided with a concave pocket or a convex briquette. There are no particular restrictions. The number of rolls and the roll diameter can be appropriately selected according to the production amount, but two rolls are generally used.

加圧造粒を少なくとも2回繰り返すと、得られる造粒二酸化チタン顔料の流動性、作業性及び分散性を調整し易いので、特に好ましい。その方法は、一旦、加圧造粒した顔料を回収し、さらに加圧造粒する、所謂、バッチ式で加圧造粒を繰り返すことでも行えるが、所望の造粒回数に相当する加圧成形機を用意して連続的に加圧造粒を繰り返すと、生産性が良く好ましい。造粒後は振動篩、サイクロン等の乾式分級機を用いて分級するのが好ましく、必要に応じて分級し易い大きさに壊砕・整粒してから分級してもよい。   It is particularly preferable to repeat the pressure granulation at least twice because the fluidity, workability and dispersibility of the resulting granulated titanium dioxide pigment can be easily adjusted. The method can be performed by collecting the pressure-granulated pigment once and further pressure-granulating, so-called batch-type pressure granulation is repeated, but pressure molding corresponding to the desired number of granulations It is preferable to prepare a machine and repeat pressure granulation continuously to improve productivity. After granulation, it is preferable to classify using a dry classifier such as a vibration sieve or a cyclone. If necessary, the particles may be classified after being crushed and sized so as to be easily classified.

以下に本発明の実施例を示すが、本発明はこれらに制限されるものではない。   Examples of the present invention are shown below, but the present invention is not limited thereto.

実施例1〜6
二酸化チタン顔料粉末としてタイペーク(登録商標)CR−50(石原産業製:酸化アルミニウム被覆)、タイペーク(登録商標)CR−50−2(石原産業製:酸化アルミニウム、多価アルコール被覆)、タイペーク(登録商標)CR−90(石原産業製:酸化アルミニウム、酸化ケイ素被覆)を用い、それぞれ20kgを、2本ロール成形機を2機用いて1.4MPaで連続的に加圧造粒した後、目開きが3mmの振動篩で分級して本発明の造粒二酸化チタン顔料を得た。これらを実施例1〜3(試料A〜C)とする。また、加圧圧力を3.4MPaに変えた以外は実施例1〜3と同様にして造粒二酸化チタン顔料を得た。これらを実施例4〜6(試料D〜F)とする。
Examples 1-6
As a titanium dioxide pigment powder, Taipei (registered trademark) CR-50 (Ishihara Sangyo: aluminum oxide coating), Taipei (registered trademark) CR-50-2 (Ishihara Sangyo: aluminum oxide, polyhydric alcohol coating), Taipei (registered) (Trademark) CR-90 (Ishihara Sangyo Co., Ltd .: Aluminum oxide, silicon oxide coating) was used for 20 kg each, continuously granulated under pressure at 1.4 MPa using two two-roll molding machines, and then opened. Was classified with a 3 mm vibrating sieve to obtain the granulated titanium dioxide pigment of the present invention. These are referred to as Examples 1 to 3 (Samples A to C). Moreover, the granulated titanium dioxide pigment was obtained like Example 1-3 except having changed the pressurization pressure into 3.4 MPa. These are designated as Examples 4 to 6 (Samples D to F).

比較例1
CR−50を水に分散させ200g/リットルの水性スラリーとした後、スプレードライヤー(FL−12型:大河原加工機製)を用い、3ミリリットル/分で入口温度230℃、出口温度120℃で噴霧乾燥して造粒した。これを比較例1(試料G)とする。
Comparative Example 1
After CR-50 is dispersed in water to form an aqueous slurry of 200 g / liter, spray drying is performed using a spray dryer (FL-12 type: manufactured by Ogawara Processing Machine Co., Ltd.) at an inlet temperature of 230 ° C. and an outlet temperature of 120 ° C. at 3 ml / min. And granulated. This is designated as Comparative Example 1 (Sample G).

比較例2
14.4kgのCR−50をプロシェアーミキサー(WB‐75型/太平洋機工製)を用い、3000回転で3分間攪拌して造粒した。これを比較例2(試料H)とする。
Comparative Example 2
14.4 kg of CR-50 was granulated by stirring for 3 minutes at 3000 rpm using a proshear mixer (WB-75 type / manufactured by Taiheiyo Kiko). This is designated as Comparative Example 2 (Sample H).

比較例3
加圧圧力を15MPaとした以外は、実施例1と同様にして比較試料の造粒酸化チタン顔料を得た。これを比較例3(試料I)とする。
Comparative Example 3
A granulated titanium oxide pigment as a comparative sample was obtained in the same manner as in Example 1 except that the pressure was changed to 15 MPa. This is designated as Comparative Example 3 (Sample I).

比較例4〜6
実施例1〜6で用いた二酸化チタン顔料粉末を比較例4〜6(試料J〜L)とする。
た。
Comparative Examples 4-6
The titanium dioxide pigment powder used in Examples 1 to 6 is referred to as Comparative Examples 4 to 6 (Samples J to L).
It was.

実施例1〜6及び比較例1〜3で得られた各試料(A〜I)の分散度及び硬度を測定した。また、実施例1〜6及び比較例1、2、4〜6の各試料(A〜H、J〜L)について、安息角、嵩密度の測定も行った。   The dispersity and hardness of each sample (A to I) obtained in Examples 1 to 6 and Comparative Examples 1 to 3 were measured. Moreover, about each sample (AH, JL) of Examples 1-6 and Comparative Examples 1, 2, 4-6, the angle of repose and the bulk density were also measured.

結果を表3に示す。本発明の造粒二酸化チタン顔料は輸送、移送、保管等の途中では造粒物がほとんど壊れることがない程度の硬度を有し、しかも造粒による分散性の低下がほとんどなく、造粒前の二酸化チタン顔料粉末の分散性が保持されていることが判る。また、二酸化チタン顔料粉末より安息角が小さいので流動性に優れ、嵩密度が大きく作業性にも優れていることが判る。噴霧乾燥や攪拌成形では硬度の高い造粒物に造粒できても、造粒前より分散性が低下していることが判る。   The results are shown in Table 3. The granulated titanium dioxide pigment of the present invention has such a hardness that the granulated product is hardly broken during transportation, transfer, storage, etc., and there is almost no decrease in dispersibility due to granulation, and before granulation. It can be seen that the dispersibility of the titanium dioxide pigment powder is maintained. Moreover, since the angle of repose is smaller than that of the titanium dioxide pigment powder, it is found that the fluidity is excellent, the bulk density is large, and the workability is also excellent. It can be seen that even if spray-drying or stirring molding can granulate a granulated product having high hardness, the dispersibility is lower than before granulation.

Figure 0004478423
Figure 0004478423

本発明の造粒二酸化チタン顔料は、分散性、流動性、作業性の何れにも優れたものであるため、このものを塗料、インキ、プラスチックス、紙等の各種組成物に配合して用いるのに有用である。
The granulated titanium dioxide pigment of the present invention is excellent in all of dispersibility, fluidity, and workability, and is used by blending it with various compositions such as paints, inks, plastics, and papers. Useful for.

Claims (3)

二酸化チタン顔料粉末をバインダーを用いずに0.1〜10MPaの範囲の圧力で加圧造粒を少なくとも2回繰り返し、加圧造粒した後の分散度を低くとも−1.5とすることを特徴とする造粒二酸化チタン顔料の製造方法。 Pressure granulation of titanium dioxide pigment powder is repeated at least twice at a pressure in the range of 0.1 to 10 MPa without using a binder, and the degree of dispersion after pressure granulation is set to at least −1.5. A method for producing a granulated titanium dioxide pigment. ロール成形機を用いて加圧造粒することを特徴とする請求項記載の造粒二酸化チタン顔料の製造方法。 Granulation method for manufacturing a titanium dioxide pigment according to claim 1, characterized in that the pressure-heading particle by using a roll molding machine. 加圧造粒した後に、分級することを特徴とする請求項記載の造粒二酸化チタン顔料の製造方法。 Pressurized heading after particle, the method for producing a granulated titanium dioxide pigment according to claim 1, wherein the classifying.
JP2003336074A 2003-09-26 2003-09-26 Method for producing granulated titanium dioxide pigment Expired - Fee Related JP4478423B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003336074A JP4478423B2 (en) 2003-09-26 2003-09-26 Method for producing granulated titanium dioxide pigment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2003336074A JP4478423B2 (en) 2003-09-26 2003-09-26 Method for producing granulated titanium dioxide pigment

Publications (2)

Publication Number Publication Date
JP2005104997A JP2005104997A (en) 2005-04-21
JP4478423B2 true JP4478423B2 (en) 2010-06-09

Family

ID=34532329

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003336074A Expired - Fee Related JP4478423B2 (en) 2003-09-26 2003-09-26 Method for producing granulated titanium dioxide pigment

Country Status (1)

Country Link
JP (1) JP4478423B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008545848A (en) * 2005-06-06 2008-12-18 マニユフアクチヤリング・アンド・プロセス・テクノロジーズ・エルエルシー(デイー/ビー/エイ エムピー テクノロジーズ) Method for forming pigment pseudo-particles
US8308800B2 (en) * 2010-04-09 2012-11-13 Chu Milton W Intraocular lenses with high contrast haptics, materials, and methods
JP2014196493A (en) * 2014-04-11 2014-10-16 マニユフアクチヤリング・アンド・プロセス・テクノロジーズ・エルエルシー(デイー/ビー/エイ エムピー テクノロジーズ) Method of forming pigment pseudo-particle
CN114106591B (en) * 2021-12-01 2023-08-29 龙佰集团股份有限公司 Preparation method of special titanium white for high-grade automotive finishing paint

Also Published As

Publication number Publication date
JP2005104997A (en) 2005-04-21

Similar Documents

Publication Publication Date Title
AU711243B2 (en) Process for producing briquetted and pressed granular material and use thereof
CA2229086C (en) Inorganic pigment pellets for coloring plastics, lacquers and building materials and a process for the production thereof
EP2054468B1 (en) Ultra fine nepheline syenite powder and products for using same
US20100154680A1 (en) Pigment granules which contain inorganic filter aids
CA2124849A1 (en) Process for particle adsorption
JP2010006629A (en) Titanium dioxide fine particle and method for producing the same
JP4235277B2 (en) Pigment granules, their production and use
US20120263954A1 (en) Nepheline syenite powder with controlled particle size and novel method of making same
JP4478423B2 (en) Method for producing granulated titanium dioxide pigment
EP2702105A1 (en) Treated inorganic pigments having improved bulk flow
US6908675B1 (en) Process to reduce dusting and improve flow properties of pigments and powders
US8349441B2 (en) Pyrogenic titanium dioxide compressed to slugs
CA2610864C (en) Methods for forming pigment pseudoparticles
US7566497B2 (en) Method for forming pigment pseudoparticles
JPH04275958A (en) Method for coloring construction material
JP2941359B2 (en) Amorphous silica filler with excellent dispersibility
US20240309216A1 (en) Method for Agglomerating Pigments and Powders
WO2012148886A1 (en) Treated inorganic pigments having improved bulk flow and their use in coating compositions
Uluçay Preparation and characterization of sterically and electrostatically stabilized TiO2 suspensions
Simon et al. NANOREP-Nanosized Particles for Improved Scratch Resistance of Polymeric Materials

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20060522

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20091113

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20091124

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20100112

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20100216

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20100315

R151 Written notification of patent or utility model registration

Ref document number: 4478423

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R151

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130319

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140319

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

LAPS Cancellation because of no payment of annual fees