JP2008527116A - ガラス様多糖類の粒子サイズを縮小する方法 - Google Patents
ガラス様多糖類の粒子サイズを縮小する方法 Download PDFInfo
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- JP2008527116A JP2008527116A JP2007550645A JP2007550645A JP2008527116A JP 2008527116 A JP2008527116 A JP 2008527116A JP 2007550645 A JP2007550645 A JP 2007550645A JP 2007550645 A JP2007550645 A JP 2007550645A JP 2008527116 A JP2008527116 A JP 2008527116A
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- glass
- polysaccharide
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- polysaccharides
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- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28002—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their physical properties
- B01J20/28004—Sorbent size or size distribution, e.g. particle size
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
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- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2220/00—Aspects relating to sorbent materials
- B01J2220/40—Aspects relating to the composition of sorbent or filter aid materials
- B01J2220/48—Sorbents characterised by the starting material used for their preparation
- B01J2220/4812—Sorbents characterised by the starting material used for their preparation the starting material being of organic character
- B01J2220/4825—Polysaccharides or cellulose materials, e.g. starch, chitin, sawdust, wood, straw, cotton
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Abstract
Description
材料
直径約2mm〜約8mm、水分含有量10%のガラス様の等級A小麦デンプンペレットをArcher Daniels Midland(登録商標)(Decatur, USA, Division Candiac, Canada)から入手した。直径約2mm〜約8mm、水分含有量8%のガラス様コーンスターチペレットをGroupe Lysac Inc.(登録商標)(Boucherville, Canada)から入手した。
ガラス様多糖類粒子はModern Processing Equipment (Chicago, USA)製のGran−U−Lizer(商標)1052 TP粉砕機を使用して縮小した。この粉砕機は3対のローラーを備えていた。ローラーは、遠心鋳造二重金属チルド鋳鉄で製作され、直径10インチ、長さ52インチであった。さらに、ローラーは波形歯で凹凸が付けられていた。ローラーは空気圧制御されて、可変の隙間調節ができるようになっていた。すべてのローラー対は、同期されておらず、すなわち異なる速度で回転した。第1のローラー対は、それぞれ478rpmおよび1160rpmの速度で回転した。第2のローラー対は、それぞれ512rpmおよび1160rpmの速度で回転した。第3のローラー対は、それぞれ614rpmおよび1160rpmの速度で回転した。25HPのモーターが各ローラー対に動力を供給した。粉砕機にはModern Processing Equipment (Chicago, USA)製、可変速度モーター駆動の1052PFローラーフィーダー(1HP)で供給した。
サンプルは、回転数1725rpmのTyler Ro−Tap(登録商標)試験用シーブシェーカーを使用して約10分間ふるい分けた。サンプルは、20、30、60および100のTylerメッシュの開口を有するふるいを用いてふるい分けた。
Modern Superabsorbent Polymer Technology (Buchholz, F.L. and Graham, A. T. Eds.、Wiley−VCH、New York、1998, section 4.6.1 Swelling Capacity: Theory and Practice、147頁)、において論じられているように、いくつかの測定方法がポリマーの膨潤能力を特徴付けるために使用されている。高吸収性材料の分野においては、重量測定膨潤能力(Gravimetric Swelling Capacity)[自由膨潤能力(Free Swell Capacity (FSC))とも呼ばれる]および遠心分離能力(Centrifuge Capacity)[遠心分離保持能力(Centrifuge Retention Capacity (CRC))とも呼ばれる]が推奨される方法である。FSCおよびCRCは、得られた吸収材製品の膨潤能力を比較するために使用した。
ヒートシール可能なAhlstrom(商標)フィルターペーパー(16.5±0.5g/m2)でティーバッグ(10×10cm)を作成した。
0.9%NaCl溶液中の自由膨潤能力(FSC)をEDANAから推奨された試験方法440.2−02によって測定した。
0.9%NaCl溶液中の遠心分離保持能力(CRC)をEDANAから推奨された試験方法441.2−02によって測定した。
(実施例1)
小麦デンプン
第1のローラー対の隙間を0.018インチ(457μm)に調節し;第2のローラー対の隙間を0.010インチ(254μm)に調節し;第3のローラー対の隙間を0.006インチ(152μm)に調節した。第1のローラー対と第2のローラー対に対して計算した侵襲性比は1.80であり;第2のローラー対と第3のローラー対に対して計算した侵襲性比は1.67であった。
粒子サイズ分布に関する隙間の効果
本明細書の以下の表2に示すように隙間を変更した。ガラス様小麦デンプンペレットをミル中に供給した。
コーンスターチのガラス様多糖類および吸収材の性質
第1ローラー対の隙間を0.0235インチ(596μm)に調節し;第2ローラー対の隙間を0.0115インチ(292μm)に調節し;第3ローラー対の隙間を0.0085インチ(216μm)に調節した。第1ローラー対と第2ローラー対に対して計算した侵襲性比は2.04であり;第2ローラー対と第3ローラー対に対して計算した侵襲性比は1.35であった。
Claims (25)
- a)0%〜約13%の水分含有量を有するガラス様多糖類およびガラス状態のガラス様多糖類からなる群から選択されたガラス様多糖類の粒子を準備するステップ、
b)前記粒子に、少なくとも3対の逐次ローラーのサイズ縮小処理を実施してサイズ縮小された粒子を生成させるステップ
を含むガラス様多糖類粒子を縮小する方法。 - 前記水分含有量が約7%〜約9%である、請求項1に記載の方法。
- 前記サイズ縮小された粒子をふるい分けする、請求項1に記載の方法。
- 前記ローラー近傍に浮遊している粒子を除去するステップをさらに含む、請求項3に記載の方法。
- 前記空気中に浮遊する粒子を除塵機を使用して除去する、請求項4に記載の方法。
- 前記ガラス様多糖類粒子がデンプンを含む、請求項1に記載の方法。
- 前記デンプンが、コーン、ワキシーコーン、小麦、ワキシー小麦、米、もち米、ポテト、キャッサバ、ワキシートウモロコシ、ソルガム、ワキシーソルガム、サゴ、そば、豆、エンドウ豆、ライ麦、大麦、アマランスおよびこれらの混合物からなる群から選択される、請求項6に記載の方法。
- 2対の逐次ローラーのそれぞれが、約1.0〜約2.0の範囲内の侵襲性比を有する、請求項1に記載の方法。
- 2対の逐次ローラーのそれぞれが、約1.2〜約1.8の範囲内の侵襲性比を有する、請求項8に記載の方法。
- 前記粒子がペレット形状である、請求項1に記載の方法。
- 前記ペレット形状の粒子が、約2mm〜約8mmの範囲内のサイズを有する、請求項10に記載の方法。
- 請求項1に記載の方法によって得られた粒子状材料。
- 微粒子含有量が約5%未満であるサイズ分布を有する、請求項12に記載の粒子状材料。
- 微粒子含有量が約2%未満であるサイズ分布を有する、請求項13に記載の粒子状材料。
- 大粒子含有量が約5%未満であるサイズ分布を有する、請求項12に記載の粒子状材料。
- 大粒子含有量が約2%未満であるサイズ分布を有する、請求項15に記載の粒子状材料。
- 請求項12に記載の粒子状材料および少なくとも1つの共吸収材料を含む吸収材組成物。
- 前記共吸収材料が、合成高吸収性ポリマー、マンノース系多糖類、イオン性多糖類、繊維およびこれらの混合物からなる群から選択される、請求項17に記載の吸収材組成物。
- 前記合成高吸収性ポリマーが、アクリル酸、アクリル酸塩、アクリル酸エステル、無水アクリル酸、メタクリル酸、メタクリル酸塩、メタクリル酸エステル、無水メタクリル酸、無水マレイン酸、マレイン酸塩、マレイン酸エステル、アクリルアミド、アクリロニトリル、ビニルアルコール、ビニルピロリドン、酢酸ビニル、ビニルグアニジン、アスパラギン酸、アスパラギン酸塩およびこれらの混合物からなる群から選択されたモノマーの重合によって得られる、請求項18に記載の吸収材組成物。
- 前記マンノース系多糖類が、グアー、タラ、ローカストビーン、コンニャク、コロハ抽出物、メスキート抽出物、アロエマンナンおよびこれらの混合物からなる群から選択される、請求項18に記載の吸収材組成物。
- 前記イオン性多糖類が、カルボキシアルキル化多糖類、酸化多糖類、硫酸化多糖類、多糖類の第四級アンモニウム誘導体、グアニジン化多糖類、キトサン、ペクチン、アラビアガム、カラヤガム、キサンタン、κ、ιまたはλ−カラギーナン、寒天、アルギン酸塩およびこれらの混合物からなる群から選択される、請求項18に記載の吸収材組成物。
- 前記繊維が、セルロース、ビスコース、レーヨン、酢酸セルロース、ナイロン(登録商標)、ポリアルキレン、ポリエチレン、ポリプロピレン、二成分繊維、ポリエステル、ポリラクチド、ポリプロパンジオール、リヨセル(商標)、ミズゴケおよびこれらの混合物からなる群から選択される、請求項18に記載の吸収材組成物。
- 使い捨て衛生用品、エアレイド不織布、家庭用品、シール材料、保湿材、採鉱および石油掘削、凝結防止塗料、水貯蔵材料、吸収性紙製品、外科用吸収材、吸収材被覆、包帯および外科用パッド、ペット用トイレ、流出化学品吸収材、化粧品用および医薬品用ポリマーゲル、人口雪、消火用ゲル、および食品包装からなる群から選択される用途における使用のための、請求項18に記載の吸収材組成物。
- 生理学的液体、生理食塩水、水および水溶液からなる群から選択された液体を吸収するための、請求項17および18に記載の吸収材組成物。
- 前記粒子に、少なくとも4対の逐次ローラーのサイズ縮小処理を実施してサイズ縮小された粒子を生成させる、請求項1に記載の方法。
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- 2005-01-13 CA CA002492884A patent/CA2492884A1/en not_active Abandoned
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2006
- 2006-01-13 JP JP2007550645A patent/JP5546729B2/ja active Active
- 2006-01-13 BR BRPI0606114-1A patent/BRPI0606114A2/pt not_active Application Discontinuation
- 2006-01-13 EP EP06704377A patent/EP1848536B1/en active Active
- 2006-01-13 US US11/813,741 patent/US20080194402A1/en not_active Abandoned
- 2006-01-13 WO PCT/CA2006/000048 patent/WO2006074556A1/en active Application Filing
- 2006-01-13 MX MX2007008597A patent/MX2007008597A/es active IP Right Grant
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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JP2019523795A (ja) * | 2016-05-31 | 2019-08-29 | ビーエーエスエフ ソシエタス・ヨーロピアBasf Se | 水性ポリマーゲルを乾燥し、乾燥されたポリマーゲルを破砕して乾燥されたポリマー粒子を得るためのベルト乾燥機装置、および水性ポリマーゲルを乾燥し、乾燥されたポリマーゲルを破砕して乾燥されたポリマー粒子を得るための方法 |
JP7021116B2 (ja) | 2016-05-31 | 2022-02-16 | ビーエーエスエフ ソシエタス・ヨーロピア | 水性ポリマーゲルを乾燥し、乾燥されたポリマーゲルを破砕して乾燥されたポリマー粒子を得るためのベルト乾燥機装置、および水性ポリマーゲルを乾燥し、乾燥されたポリマーゲルを破砕して乾燥されたポリマー粒子を得るための方法 |
Also Published As
Publication number | Publication date |
---|---|
CA2492884A1 (en) | 2006-07-13 |
WO2006074556A1 (en) | 2006-07-20 |
MX2007008597A (es) | 2008-01-11 |
EP1848536B1 (en) | 2012-05-16 |
JP2014141685A (ja) | 2014-08-07 |
JP5546729B2 (ja) | 2014-07-09 |
EP1848536A1 (en) | 2007-10-31 |
US20080194402A1 (en) | 2008-08-14 |
EP1848536A4 (en) | 2009-03-04 |
BRPI0606114A2 (pt) | 2009-06-02 |
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