CN100519632C - 精细颗粒的聚亚芳基醚酮粉末 - Google Patents
精细颗粒的聚亚芳基醚酮粉末 Download PDFInfo
- Publication number
- CN100519632C CN100519632C CNB2005101369029A CN200510136902A CN100519632C CN 100519632 C CN100519632 C CN 100519632C CN B2005101369029 A CNB2005101369029 A CN B2005101369029A CN 200510136902 A CN200510136902 A CN 200510136902A CN 100519632 C CN100519632 C CN 100519632C
- Authority
- CN
- China
- Prior art keywords
- powder
- paek
- polyarylidenetherketpowder
- ether ketone
- polyarylene ether
- 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.)
- Active
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/02—Making granules by dividing preformed material
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/12—Powdering or granulating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B13/00—Conditioning or physical treatment of the material to be shaped
- B29B13/10—Conditioning or physical treatment of the material to be shaped by grinding, e.g. by triturating; by sieving; by filtering
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G65/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G65/34—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from hydroxy compounds or their metallic derivatives
- C08G65/46—Post-polymerisation treatment, e.g. recovery, purification, drying
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L71/00—Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L71/00—Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
- C08L71/08—Polyethers derived from hydroxy compounds or from their metallic derivatives
- C08L71/10—Polyethers derived from hydroxy compounds or from their metallic derivatives from phenols
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B9/00—Making granules
- B29B9/12—Making granules characterised by structure or composition
- B29B2009/125—Micropellets, microgranules, microparticles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
- B29K2071/00—Use of polyethers, e.g. PEEK, i.e. polyether-etherketone or PEK, i.e. polyetherketone or derivatives thereof, as moulding material
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G2650/00—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
- C08G2650/28—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type
- C08G2650/38—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing oxygen in addition to the ether group
- C08G2650/40—Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule characterised by the polymer type containing oxygen in addition to the ether group containing ketone groups, e.g. polyarylethylketones, PEEK or PEK
Landscapes
- Chemical & Material Sciences (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- Mechanical Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Organic Chemistry (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
- Crushing And Grinding (AREA)
- Paints Or Removers (AREA)
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Crushing And Pulverization Processes (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Polyethers (AREA)
Abstract
本发明涉及一种制备细颗粒聚亚芳基醚酮的方法,其特征在于,研磨BET表面积大于1m2/g的多孔聚亚芳基醚酮。
Description
技术领域
本发明涉及一种精细颗粒的聚亚芳基醚酮(PAEK),通过研磨多孔PAEK来制备其的方法以及该产品的应用。
背景技术
用各种研磨装置和研磨方法来研磨聚合物已是一种公知的技术,其已被用于各种各样的研磨产品,例如用于聚酯、聚酰胺或聚烯烃。这些聚合物通常以低温研磨法而从相应的市售得到的颗粒形式研磨成相应的粉末。为此,通常要在最低-60℃的操作温度下使用针磨机(Stiftmühlen)或流动床研磨机。PAEK,特别是还有聚醚醚酮(PEEK)还表现出突出的摩擦性能和机械性能;所以它们很难且需要耗费较高成本才能研磨成精细粉末。在DE3844457A1中记载了在流动床研磨机上冷磨PAEK的方法,其中得到平均粒径为40μm或更小的精细粉末。但这里的缺点是产率至多只有7.5kg/h,明显低于研磨装置的常规产量。研磨PAEK的技术困难是显然的。
因此存在着一些偶然的开端方法,其在粉末制备中避开了研磨步骤而以一些替代路线得到了粉末状或精细粉末状的PAEK。在US5910558中记载了通过对熔体喷射造粒或通过对溶液喷雾干燥而制备PAEK超细粉的方法。但是这种方法由于高设备成本和低的加工稳定性而无法推广。
另一公开于WO99/50339中的方法是将PAEK和其他聚合物相混合并因此赋予PAEK颗粒形式。在将其他聚合物溶于合适的溶剂中之后,就能得到粉末状的PAEK。但是这种方法非常昂贵。
发明内容
由此出发,本发明的任务在于提供一种具有更好研磨产率且成本较低的研磨方法,以制备精细颗粒的PAEK粉末。
该任务的解决方法是将BET表面积大于1m2/g,优选大于4m2/g,特别优选大于8m2/g且特别优选大于12m2/g的多孔PAEK研磨成粉末。
多孔PAEK的制备方法通常是,使芳族二卤化物与双酚和/或卤代酚,在碱金属或碱土金属的碳酸盐或它们的碳酸氢盐存在的条件下且在高沸点的质子惰性溶剂中反应生成PAEK,卸出熔体并使其凝固,任选地还要在例如锤磨机中进行研磨,用一种或多种有机溶剂萃取所形成的颗粒以去除反应溶剂以及用水萃取以出去无机盐,接着进行干燥。要萃取的颗粒除了通过研磨外还可通过对挤出条材进行造粒,涂覆液滴于冷却的金属带上,造粒或喷雾干燥由反应混合物制得。萃取后所得到的孔隙率特别要取决于在萃取物中的反应溶剂的含量。优选使得在喷雾干燥过程中只有一部分反应溶剂被除去。此外,要萃取颗粒的制备方式不起决定性作用。
带有接着的萃取过程的PAEK制备方法记载于大量的专利申请中,例如EP-A-0001879,EP-A-0182648,EP-A-0244167和EP-A-0322151。
但在本发明范畴内,可以另一种方法制得且以紧密形式,例如颗粒形式存在的PAEK也可溶于合适的高沸点质子惰性溶剂中,由此,该热溶液也如上面针对反应所得的熔体所述的内容那样转变为颗粒形式并用一种或多种有机溶剂萃取。
根据现有技术,高沸点的质子惰性溶剂优选是具有如下通式的化合物
其中,T表示直接连接、氧原子或两个氢原子;Z和Z’是氢或苯基。这里优选指的是二苯砜。
PAEK含有具有以下结构式的单元
(-Ar-X-)和(-Ar’-Y-),
其中,Ar和Ar’表示二价芳基,优选是1,4-亚苯基、4,4’-联苯撑(Biphenylen)以及1,4-,1,5-或2,6-亚萘基。X是吸电子基团,优选是羰基或磺酰基,而Y是其他基团,如O、S、CH2、异亚丙基或类似物。其中,至少50%、优选至少70%、特别优选至少80%的基团X应该为羰基,而至少50%、优选至少70%且特别优选至少80%的基团Y应由氧组成。
在特别优选的实施方式中,100%的基团X由羰基组成而100%的基团Y由氧组成。在该实施方式中,PAEK可以是例如聚醚醚酮(PEEK;式I),聚醚酮(PEK;式II),聚醚酮酮(PEKK;式III)或聚醚醚酮酮(PEEKK;式IV),但是其自然也可以是羰基和氧基的其他排列结构。
所述PAEK通常是部分结晶的,其表现为,例如可在DSC分析中检测到晶体熔融点Tm,并且该值在大多数情况下为约300℃或更高。但本发明教导也可使用非晶态的PAEK。通常,磺酰基、联苯撑基团、亚萘基或大体积基Y例如异亚丙基都能减少结晶度。
在一个优选实施方式中,根据DIN EN ISO 307,于25℃下且在250mg的PAEK于50ml 96重量%的H2SO4中形成的溶液中测量粘度值,测得该值为约20至150cm3/g且优选为50至120cm3/g。
根据DIN ISO 9277来确定BET表面积。
在室温或更高温度下研磨多孔PAEK,但为了改善研磨过程和研磨产率,有利的是在较低温度下研磨,更优选低于0℃,特别优选低于-20℃且极其优选低于-40℃。特别地,针磨机、流动床喷射研磨机或冲击研磨机都适合于研磨过程。这里,待研磨的PAEK的多孔结构会带来在上述条件下能引起断裂的脆弱点。
接着,可以对研磨材料进行分类或过筛。根据所用研磨材料和后续分离方法,可以得到数均粒径(d50)为1至300μm、优选4至200μm、更优选10至150μm、特别优选15至120μm且极其优选20至100μm的细粉末的PAEK。在特别有益的实施方式中,以这种方法就能制得d50为15至80μm和d90为小于160μm,且优选d50为20至50μm和d90为小于100μm的细粉末的PAEK。
根据DIN ISO 13320-1通过激光衍射来测定粒径及其分布。
接着可以向PAEK粉末中添加例如干燥混合物形式的添加剂,例如无机颜料,如二氧化钛、炭黑和类似物,或加工助剂。
如此得到的精细粉末PAEK可以通过静电涂覆、流化床烧结或用PAEK水悬浮液进行涂覆的方法而被用于涂覆例如金属(例如钢)物件或陶瓷物件。在这些情况下,其中可以含有作为无机加工助剂的例如Al2O3或SiO2(如二氧化硅气溶胶(Aerosil))。此外,其还适于,例如通过用粉末浸渍增强纤维织物和接着在足够高的温度下压制的方法来制备复合材料。另外,其也可以例如通过烧结或恒热压制而加工成模制体。
具体实施方式
以下将通过实施例来阐释本发明。
实施例1:
利用低温工作的针磨机(Hosokawa Alpine CW 160)来研磨具有50m2/gBET表面积和500μm平均粒径的PEEK颗粒。该过程中,经由一个输送螺杆将PEEK颗粒输送到研磨室内,与此同时用液氮冷却至-50℃。在该研磨室内,通过旋转的针盘将PEEK颗粒加速到220m/s。在该速度下,它们会喷射到安置在针盘上的针头,并且因此会受到强烈的使颗粒破裂的喷射应力。这一过程发生在PEEK颗粒的通量为15kg/h的情况下。离开研磨室后的微粉化了的产品有30重量%的颗粒小于100μm(根据DIN EN ISO 4610利用Alpine空气喷射筛进行筛网分析得到)。
在微粉化之后接着进行分离操作步骤。其中,要借助于Alpine空气喷射筛且利用下游连接的旋风分离器(Zyklon)来分离微细化的PEEK颗粒。在80μm的筛目大小下进行分离过程。如此得到的粉末的特征在于d10为16.7μm,d50为52.6μm且d90为113.8μm。
实施例2:
如实施例1进行操作,但通量为20kg/h。离开研磨室后的微粉化了的产品有30重量%的颗粒小于100μm。
在微粉化之后接着进行分离操作步骤。其中,要借助于之字形分级机来分离微细化的PEEK颗粒。之字形分级机的操作参数为:转速10000min-1,载气量为65m3/h。如此得到的粉末的特征在于d10为8.5μm,d50为21.4μm且d90为54.9μm。
比较例1:
试验利用低温工作的针磨机(Hosokawa Alpine CW 160)来研细PEEK颗粒(BET表面积小于0.1m2/g)。该过程中,经由一个输送螺杆将PEEK颗粒输送到研磨室内,与此同时用液氮冷却至-70℃。在该研磨室内,通过旋转的针盘将PEEK颗粒加速到220m/s。在该速度下,它们会喷射到安置在针盘上的针头,并且会受到强烈的喷射应力。PEEK颗粒的通量为15kg/h。离开研磨室后的产品有2重量%的颗粒小于100μm。进行三次该过程之后,得到7重量%的产品小于100μm。由于在研磨时作用度较低,因此放弃分离过程。
Claims (11)
1.制备聚亚芳基醚酮粉末的方法,其特征在于,研磨BET表面积大于1m2/g的多孔聚亚芳基醚酮。
2.如权利要求1所述的方法,其特征在于,在低于0℃的温度下研磨多孔聚亚芳基醚酮。
3.如权利要求1所述的方法,其特征在于,对研磨的产品进行分离或筛分。
4.如权利要求2所述的方法,其特征在于,对研磨的产品进行分离或筛分。
5.如权利要求3所述的方法,其特征在于,所得到的聚亚芳基醚酮粉末具有d50为1至300μm的数均粒径。
6.如权利要求4所述的方法,其特征在于,所得到的聚亚芳基醚酮粉末具有d50为1至300μm的数均粒径。
7.如权利要求1-6之一所述的方法,其特征在于,聚亚芳基醚酮是PEEK,PEK,PEKK或PEEKK。
8.如权利要求1-6之一所述的方法,其特征在于,聚亚芳基醚酮具有20至150cm3/g的粘度值。
9.根据权利要求1-8之一所述的方法制得的聚亚芳基醚酮粉末。
10.如权利要求9所述的聚亚芳基醚酮粉末,其特征在于,其含有混入的无机颜料或加工助剂。
11.如权利要求9和10之一所述的聚亚芳基醚酮粉末的用途,用于涂覆或制备复合材料或模制体。
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102004062762.2 | 2004-12-21 | ||
DE102004062762A DE102004062762A1 (de) | 2004-12-21 | 2004-12-21 | Feinkörniges Polyarylenetherketonpulver |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1800242A CN1800242A (zh) | 2006-07-12 |
CN100519632C true CN100519632C (zh) | 2009-07-29 |
Family
ID=35976559
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2005101369029A Active CN100519632C (zh) | 2004-12-21 | 2005-12-20 | 精细颗粒的聚亚芳基醚酮粉末 |
Country Status (9)
Country | Link |
---|---|
US (1) | US7875234B2 (zh) |
EP (1) | EP1833878A1 (zh) |
JP (1) | JP4922183B2 (zh) |
KR (1) | KR100901906B1 (zh) |
CN (1) | CN100519632C (zh) |
BR (1) | BRPI0519137A2 (zh) |
DE (1) | DE102004062762A1 (zh) |
RU (1) | RU2414483C2 (zh) |
WO (1) | WO2006067017A1 (zh) |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102004062761A1 (de) * | 2004-12-21 | 2006-06-22 | Degussa Ag | Verwendung von Polyarylenetherketonpulver in einem dreidimensionalen pulverbasierenden werkzeuglosen Herstellverfahren, sowie daraus hergestellte Formteile |
DE102007016656B4 (de) * | 2007-04-05 | 2018-10-11 | Eos Gmbh Electro Optical Systems | PAEK-Pulver, insbesondere zur Verwendung in einem Verfahren zum schichtweisen Herstellen eines dreidimensionalen Objektes, sowie Verfahren zu dessen Herstellung |
ES2640732T3 (es) * | 2008-05-21 | 2017-11-06 | Toray Industries, Inc. | Método de producción de partícula fina de polímero |
GB0813093D0 (en) * | 2008-07-17 | 2008-08-27 | Invibio Ltd | Polymeric materials |
FR2982519B1 (fr) | 2011-11-10 | 2020-02-21 | Arkema France | Procede de broyage de polyaryl ether cetones |
CN103566827A (zh) * | 2012-07-12 | 2014-02-12 | 金发科技股份有限公司 | 一种均相溶液聚合的高分子聚合物及其精制方法 |
WO2014100320A1 (en) | 2012-12-19 | 2014-06-26 | Oxford Performance Materials, Inc. | Method for preparing fine powders for use in selective laser sintering processes |
WO2014130275A2 (en) | 2013-02-22 | 2014-08-28 | Ticona Llc | High performance polymer composition with improved flow properties |
FR3015506B1 (fr) * | 2013-12-20 | 2017-04-21 | Arkema France | Composition de poudres de poly-arylene-ether-cetone-cetones autorisant un excellent compromis coulabilite et coalescence adaptees au frittage laser |
GB2526243B (en) | 2014-02-24 | 2021-07-14 | Victrex Mfg Ltd | Polymeric materials |
CN106574184A (zh) | 2014-08-21 | 2017-04-19 | 提克纳有限责任公司 | 包含聚芳基醚酮和低环烷液晶聚合物的组合物 |
EP3183321A1 (en) | 2014-08-21 | 2017-06-28 | Ticona LLC | Polyaryletherketone composition |
WO2016057253A1 (en) | 2014-10-08 | 2016-04-14 | Ticona Llc | Dispersant for use in synthesis of polyaryletherketones |
FR3027834B1 (fr) | 2014-11-03 | 2017-11-10 | Arkema France | Procede de densification de poudres de polyarylene-ether-cetone |
KR102613603B1 (ko) * | 2015-12-28 | 2023-12-15 | 알케마 인코포레이티드 | 중합체 분말의 제조 방법 |
US11352480B2 (en) | 2016-03-18 | 2022-06-07 | Ticona Llc | Polyaryletherketone composition |
PL3293232T3 (pl) | 2016-09-08 | 2021-01-25 | Igp Pulvertechnik Ag | Farba proszkowa i sposób wytwarzania farby proszkowej |
JP7046489B2 (ja) | 2017-01-06 | 2022-04-04 | 住友化学株式会社 | 樹脂微粒子の製造方法、樹脂粒子 |
CN107674560A (zh) * | 2017-10-31 | 2018-02-09 | 山东凯盛新材料股份有限公司 | 聚醚酮酮抗静电喷涂粉末涂料的制备方法 |
CN107618122B (zh) * | 2017-10-31 | 2019-08-30 | 山东凯盛新材料股份有限公司 | 聚醚酮酮细粉的制备方法 |
US11118053B2 (en) | 2018-03-09 | 2021-09-14 | Ticona Llc | Polyaryletherketone/polyarylene sulfide composition |
JP7338316B2 (ja) * | 2018-08-31 | 2023-09-05 | 株式会社リコー | 樹脂粉末、及び立体造形物の製造方法 |
EP3917989A1 (en) | 2019-01-31 | 2021-12-08 | Solvay Specialty Polymers USA, LLC. | Method of grinding poly(ether ketone ketone) (pekk) |
US20200247012A1 (en) * | 2019-02-05 | 2020-08-06 | Scott DeFelice | Method for Grinding Materials for Additive Manufacturing |
RU2691409C1 (ru) * | 2019-02-18 | 2019-06-13 | Российская Федерация, от имени которой выступает ФОНД ПЕРСПЕКТИВНЫХ ИССЛЕДОВАНИЙ | Способ получения термостойких ароматических полиэфирэфир- и сополиэфирэфиркетонов с улучшенными физико-механическими характеристиками |
FR3127496A1 (fr) | 2021-09-28 | 2023-03-31 | Arkema France | Poudre à base de polyaryléthercétone(s) pour la fabrication d’objets ductiles. |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5670057A (en) * | 1979-11-12 | 1981-06-11 | Asahi Chem Ind Co Ltd | Preparation of powdered resin composition |
DE3518277A1 (de) | 1984-10-06 | 1986-04-10 | Hüls AG, 4370 Marl | Thermoplastische massen auf basis von polyphenylenethern und polyoctenylenen sowie verfahren zu ihrer herstellung |
DE3844457A1 (de) | 1988-12-31 | 1990-07-12 | Hoechst Ag | Feinkoerniges polyetherketonpulver, verfahren zu dessen herstellung und dessen verwendung |
US5247052A (en) * | 1988-12-31 | 1993-09-21 | Hoechst Aktiengesellschaft | Fine-grained polyether-ketone powder, process for the manufacture thereof, and the use thereof |
JPH08323748A (ja) * | 1995-05-29 | 1996-12-10 | Toho Rayon Co Ltd | 成形材料及びその製造方法 |
JPH11320691A (ja) * | 1998-05-21 | 1999-11-24 | Tosoh Corp | 熱可塑性樹脂パウダー及びそれよりなる成形体 |
JP4152521B2 (ja) * | 1999-04-16 | 2008-09-17 | 旭化成ケミカルズ株式会社 | 粒度分布の改良されたポリフェニレンエーテル粉体の製造法 |
WO2003050163A1 (fr) | 2001-12-11 | 2003-06-19 | Mitsui Chemicals, Inc. | Cetone de polyether et procede de production |
JP2004203919A (ja) * | 2002-12-24 | 2004-07-22 | Inoac Corp | 熱可塑性樹脂パウダーの製造方法 |
US20050207931A1 (en) * | 2004-03-21 | 2005-09-22 | Toyota Motorsport Gmbh | unknown |
DE102004062761A1 (de) | 2004-12-21 | 2006-06-22 | Degussa Ag | Verwendung von Polyarylenetherketonpulver in einem dreidimensionalen pulverbasierenden werkzeuglosen Herstellverfahren, sowie daraus hergestellte Formteile |
-
2004
- 2004-12-21 DE DE102004062762A patent/DE102004062762A1/de not_active Withdrawn
-
2005
- 2005-11-22 BR BRPI0519137-8A patent/BRPI0519137A2/pt not_active Application Discontinuation
- 2005-11-22 KR KR1020077013935A patent/KR100901906B1/ko active IP Right Grant
- 2005-11-22 JP JP2007546009A patent/JP4922183B2/ja active Active
- 2005-11-22 WO PCT/EP2005/056153 patent/WO2006067017A1/de active Application Filing
- 2005-11-22 RU RU2007127795/05A patent/RU2414483C2/ru active
- 2005-11-22 US US11/722,261 patent/US7875234B2/en active Active
- 2005-11-22 EP EP05816251A patent/EP1833878A1/de not_active Withdrawn
- 2005-12-20 CN CNB2005101369029A patent/CN100519632C/zh active Active
Also Published As
Publication number | Publication date |
---|---|
RU2414483C2 (ru) | 2011-03-20 |
KR20070089178A (ko) | 2007-08-30 |
WO2006067017A1 (de) | 2006-06-29 |
BRPI0519137A2 (pt) | 2008-12-23 |
US20090280263A1 (en) | 2009-11-12 |
CN1800242A (zh) | 2006-07-12 |
RU2007127795A (ru) | 2009-01-27 |
US7875234B2 (en) | 2011-01-25 |
EP1833878A1 (de) | 2007-09-19 |
JP4922183B2 (ja) | 2012-04-25 |
JP2008524356A (ja) | 2008-07-10 |
DE102004062762A1 (de) | 2006-06-22 |
KR100901906B1 (ko) | 2009-06-10 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN100519632C (zh) | 精细颗粒的聚亚芳基醚酮粉末 | |
US11691315B2 (en) | Method of grinding polyaryletherketones | |
KR101965007B1 (ko) | 용융 유리의 제조 방법 및 유리 제품의 제조 방법 | |
EP2834217B1 (en) | Nicotinamide powder and process and device for its production | |
KR20140139478A (ko) | 조립체 및 그 제조 방법 | |
CN109923069A (zh) | 埃洛石粉末和埃洛石粉末的制造方法 | |
EP3202824A1 (en) | Polymer powder and method for preparing same | |
CN108675824A (zh) | 一种等离子物理气相沉积热障涂层用多孔稀土锆酸盐粉末及其制备方法 | |
CN104449787A (zh) | 一种固体颗粒沥青的生产方法 | |
CA2006904A1 (en) | Fine-grained polyether-ketone powder, process for the manufacture thereof, and the use thereof | |
JP5857063B2 (ja) | 粉砕助剤を用いてジェットミルでワックスを粉砕するための方法、粉砕助剤としてのポリオールの使用、およびポリオールを含むワックス粉末 | |
CN101209861A (zh) | 气体分离法制备氧化铁纳米材料 | |
CN111989293B (zh) | 准埃洛石粉末及准埃洛石粉末的制造方法 | |
JP5071956B2 (ja) | 薬物封入ナノ粒子の造粒物及び造粒方法 | |
JP2007091688A (ja) | 固形製剤コーティング用微粉末の製造方法 | |
CN109135826B (zh) | 一种粉状费托蜡的制备方法 | |
KR100933547B1 (ko) | 다성분계 비정질 소재의 균일한 나노 크기 입자 분쇄 방법 | |
KR20200046708A (ko) | 물에 신속하게 분산되는 가루녹차 과립의 제조방법 | |
JPS6025046B2 (ja) | 粒度分布の狭い芳香族ポリエステルの製法 | |
JP2009262061A (ja) | 微細な球形造粒物の製造方法 | |
JPH0677676B2 (ja) | 混合粉末の製造方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C56 | Change in the name or address of the patentee |
Owner name: EVONIK DEGUSSA CO., LTD. Free format text: FORMER NAME: DEGUSSA CO., LTD. |
|
CP01 | Change in the name or title of a patent holder |
Address after: Dusseldorf Patentee after: DEGUSSA GmbH Address before: Dusseldorf Patentee before: Degussa AG |
|
CP03 | Change of name, title or address |
Address after: essen Patentee after: EVONIK DEGUSSA GmbH Address before: Dusseldorf Patentee before: Degussa GmbH |