序号 专利名 申请号 申请日 公开(公告)号 公开(公告)日 发明人
61 Process for the production of water and solvent-free nitrile rubbers US13635810 2011-03-21 US09469697B2 2016-10-18 Hanns-Ingolf Paul; Paul Wagner; Rolf Feller; Jörg Kirchhoff; John Lovegrove; Florian Forner; Michael Klimpel; Peter Weuta; Sven Brandau
The present invention relates to specific water and solvent-free nitrile rubbers having specific functional groups and/or end groups, a process for the production thereof and the use thereof. This process involves removing volatile compounds from a fluid (F) containing (1) at least one nitrile rubber and (2) at least one volatile compound, wherein the process comprises at least the steps of a.) treating the fluid (F) in at least one conversation unit, b.) retreating the concentrated fluid from step a.) in at least one retreating unit and c.) feeding the retreated concentrated fluid from step b.) into at least one retreating unit.
62 PROCESS FOR THE PRODUCTION OF WATER AND SOLVENT-FREE HYDROGENATED NITRILE RUBBERS US14976278 2015-12-21 US20160145425A1 2016-05-26 Matthias SODDEMANN; Werner OBRECHT; Franz-Josef MERSMANN; Hanns-Ingolf PAUL; Paul WAGNER; Rolf FELLER; Thomas KOENIG; Jorg KIRCHHOFF; John LOVEGROVE
The present invention relates to a process for the production of water and solvent-free hydrogenated nitrile rubber polymers, to the hydrogenated nitrile rubbers and the use thereof.
63 Process for the production of water and solvent-free hydrogenated nitrile rubbers US13874930 2013-05-01 US09249236B2 2016-02-02 Matthias Soddemann; Werner Obrecht; Franz-Josef Mersmann; Hanns-Ingolf Paul; Paul Wagner; Rolf Feller; Thomas Koenig; Jorg Kirchhoff; John Lovegrove
The present invention relates to a process for the production of water and solvent-free hydrogenated nitrile rubber polymers, to the hydrogenated nitrile rubbers and the use thereof.
64 Method for Producing Polymer US14761356 2014-01-08 US20150353669A1 2015-12-10 Yoshifumi Araki; Eiji Sasaya; Takuya Suzuki
A method for producing a polymer has: a polymerization step of polymerizing at least a conjugated diene monomer in a hydrocarbon solvent using an organolithium compound as a polymerization initiator, and obtaining a polymer; and, following steps (1) to (4), successively performing after the polymerization step: (1) a step of mixing an acid and water of 20 to 300 parts by mass into the solution containing the polymer of 100 parts by mass, (2) a step of adjusting an amount of the water to 10 parts by mass or less based on 100 parts by mass of the solution containing the polymer, (3) a step of adding a carbon oxide gas and/or a compound to be decarboxylated to the solution containing the polymer, and (4) a step of removing a solvent from the solution containing the polymer until a concentration of the polymer reaches 95 mass % or more.
65 Process for the removal of the solvent from a polymeric solution US14357585 2012-11-23 US09090746B2 2015-07-28 Maria Parisi; Piero Maestri
A process for the removal of solvent from a polymeric solution including at least one elastomeric polymer. The polymeric solution is subjected to a stripping step by means of water vapor, in the presence of a dispersant system including: from 0.005% by weight to 1% by weight, with respect to the total weight of the dry elastomeric polymer, of at least one lamellar material; from 0.0005% by weight to 1% by weight, with respect to the total weight of the dry elastomeric polymer, of at least one cationic surfactant.
66 Process for forming and devolatilizing brominated polybutadiene polymer particles US13057251 2009-08-18 US08883253B2 2014-11-11 Douglas C. Greminger; Brian D. Scherzer
Brominated butadiene polymers are recovered from solution and formed into particles by spraying the solution onto a heated, mechanically agitated bed of seed particles. The droplets contact the seed particles in the bed and form a polymer layer on the outside of the seed particles, thereby enlarging them. The solvent is removed from the droplets after they make contact with seed particles in the bed. The process allows for the simultaneous removal of solvent and formation of somewhat large particles. The process forms at most small amounts of agglomerates and fines.
67 PROCESS FOR THE REMOVAL OF THE SOLVENT FROM A POLYMERIC SOLUTION US14357585 2012-11-23 US20140323674A1 2014-10-30 Maria Parisi; Piero Maestri
A process for the removal of the solvent from a polymeric solution including at least one elastomeric polymer, which comprises subjecting said polymeric solution to a stripping step by means of water vapour, in the presence of a dispersant system comprising: —from 0.005% by weight to 1% by weight, preferably from 0.008% by weight to 0.8% by weight, with respect to the total weight of the dry elastomeric polymer, of at least one lamellar material; —from 0.0005% by weight to 1% by weight, preferably from 0.0008% by weight to 0.8% by weight, with respect to the total weight of the dry elastomeric polymer, of at least one cationic surfactant.
68 Method for Elastomer Finishing US13070078 2011-03-23 US20120071619A1 2012-03-22 Yu Feng WANG; Richard C-M Yeh
In the production of isobutylene-based elastomers the product obtained from the polymerization process is often in the form of a stream. Described herein are an apparatus and a process for removal of hydrocarbon liquids from the elastomer. The process comprises the steps of obtaining a stream comprising hydrocarbon liquids, either solvents or diluents, and an isobutylene-based elastomer; passing the stream through a kneader to volatize the hydrocarbon liquids from the elastomer.
69 PROCESS FOR THE PRODUCTION OF WATER AND SOLVENT-FREE POLYMERS US13063227 2009-09-17 US20120043687A1 2012-02-23 Jörg Kirchhoff; Werner Bäcker; Rolf Feller; Paul Wagner; John Lovegrove; Hanns-Ingolf Paul
The present invention relates to water and solvent-free polymers, in particular water and solvent-free synthetic rubber products like non-halogenated and halogenated butyl rubber products as well as a process for the production thereof. The invention further relates to a device suitable to accomplish said process.
70 PROCESS FOR FORMING AND DEVOLATILIZING BROMINATED POLYBUTADIENE POLYMER PARTICLES US13057251 2009-08-18 US20110143030A1 2011-06-16 Douglas C. Greminger
Brominated butadiene polymers are recovered from solution and formed into particles by spraying the solution onto a heated, mechanically agitated bed of seed particles. The droplets contact the seed particles in the bed and form a polymer layer on the outside of the seed particles, thereby enlarging them. The solvent is removed from the droplets after they make contact with seed particles in the bed. The process allows for the simultaneous removal of solvent and formation of somewhat large particles. The process forms at most small amounts of agglomerates and fines.
71 Method for the termination of anionic polymerization using phosphate ester/water mixture US11746796 2007-05-10 US07459507B2 2008-12-02 Sam-min Kim; Young Jin Kim; Seung Il Kim; Ji-Eun Ryu
The present invention relates to a method for terminating anionic polymerization using phosphate ester/water mixture, more particularly to a novel method for terminating anionic polymerization using phosphate ester/water mixture as a polymerization terminator in a living polymer solution prepared by the anionic polymerization, so that the polymerization can be terminated effectively, without coupling or discoloration and with less production of basic materials that affect the antioxidant, thereby enabling control of acidity without necessitating a further neutralization process.
72 METHOD FOR THE TERMINATION OF ANIONIC POLYMERIZATION USING PHOSPHATE ESTER/WATER MIXTURE US11746796 2007-05-10 US20080114137A1 2008-05-15 Sam-min KIM; Young Jin Kim; Seung Il Kim; Ji-Eun Ryu
The present invention relates to a method for terminating anionic polymerization using phosphate ester/water mixture, more particularly to a novel method for terminating anionic polymerization using phosphate ester/water mixture as a polymerization terminator in a living polymer solution prepared by the anionic polymerization, so that the polymerization can be terminated effectively, without coupling or discoloration and with less production of basic materials that affect the antioxidant, thereby enabling control of acidity without necessitating a further neutralization process.
73 Process to produce tack-free rubber particles US665927 1991-03-05 USH1094H 1992-08-04 John E. Gorman
A process to produce a free flowing fine polymer powder is provided. The process comprises the steps of: providing a polymer cement comprising a polymer either melt or dissolved in a solvent to form a polymer cement; dispersing an antiblocking agent within a stream consisting of steam to form atomization steam; atomizing the polymer cement; contacting the atomized polymer cement with the atomization steam; and recovering polymeric particles. Polymeric particles so prepared have an average particle size of between 100 and 1000 microns. In a preferred embodiment, the polymers produced are rubbery polymers which are free flowing.
74 Solvent fractionation of guayule rubber US754554 1985-07-15 US4623713A 1986-11-18 Robert T. Beinor; William M. Cole
A method and composition are disclosed wherein guayule rubber is fractionated into desirable weight average molecular weight fractions by a desired solvent system. Oftentime, a plurality of fractionating steps is utilized wherein the desirable molecular weight rubber fraction is precipitated or extracted. High weight average molecular weight rubbers having usually less than 4% by weight of resin content therein are generally desirable because of their favorable physical properties.
75 Low energy polymer-solvent separations US299744 1981-09-08 US4444922A 1984-04-24 Timothy G. Gutowski; Nam P. Suh
A method for processing a polymer solution by changing the thermodynamic state of the solution to produce a dilute phase and a concentrated phase such that the thermodynamic state is sufficiently changed that the two phases are formed by spinodal decomposition.
76 Process for improving the stability of cis-1 4-polyisoprene vulcanisates US3631016D 1970-07-20 US3631016A 1971-12-28 WITTE JOSEF; HAAS FRIEDRICH; PAMPUS GOTTFRIED; SCHON NIKOLAUS
PROCESS FOR IMPROVING THE STABILITY OF CIS-1,4-POLYISOPRENE VULCANISATES BY INACTIVATING A CATALYST CONTAINING SOLUTION OF POLYISOPRENE IN AN ORGANIC SOLVENT WITH A MIXTURE COMPRISING A LOWER ALIPHATIC ALCOHOL, A CONVENTIONAL ETABILISER AND A SMALL QUANTITY OF AN ALIPHATIC OR CYCLOALIPHATIC SECONDARY AMINE WHOSE ALKYL OR CYCLOALKYL RADICALS TOGETHER CONTAIN AT LEAST 10 CARBON ATOMS.
77 および溶媒を含まないニトリルゴムの製造方法 JP2013500453 2011-03-21 JP6289905B2 2018-03-07 ハンス−インゴルフ・パウル; パウル・ヴァグナー; ロルフ・フェラー; イェルク・キルヒホフ; ジョン・ラヴグローヴ; フローリアン・フォルナー; ミヒャエル・クリンペル; ペーター・ヴォイタ; スヴェン・ブランドー
78 および溶媒を含まないポリマーの製造方法 JP2017114945 2017-06-12 JP2017160458A 2017-09-14 ヨルク・キルヒホフ; ヴェルナー・バッカー; ロルフ・フェルラー; ポール・ヴァグナー; ジョン・ラヴグローヴ; ハンス−インゴルフ・ポール
【課題】揮発性化合物を、少なくとも1つのポリマー、好ましくは、少なくとも1つの合成ゴムを含有する流体から除去する、連続した、エネルギー効率の良い、環境的かつ経済的に好ましいプロセスを提供して、揮発性化合物を実質的に含まないポリマー生成物を生成する。
【解決手段】本発明は、および溶媒を含まないポリマー、特に、非ハロゲン化およびハロゲン化ブチルゴム生成物のような水および溶媒を含まない合成ゴム生成物、ならびにその製造方法に関する。本発明はさらに、そのプロセスを実施するのに好適な装置に関する。装置は、濃縮器ユニットと、加熱ユニットと、押出し機ユニットとを少なくとも含む。
【選択図】図1
79 および溶媒を含まないニトリルゴムの製造方法 JP2015213145 2015-10-29 JP2016026262A 2016-02-12 ハンス−インゴルフ・パウル; パウル・ヴァグナー; ロルフ・フェラー; イェルク・キルヒホフ; ジョン・ラヴグローヴ; フローリアン・フォルナー; ミヒャエル・クリンペル; ペーター・ヴォイタ; スヴェン・ブランドー
【課題】ニトリルゴムを少なくとも含有する流体から揮発性化合物を除去するためのエネルギー効率的な、環境に優しいおよび経済的に有利な方法を提供すること。
【解決手段】(1)少なくとも1つのニトリルゴムおよび(2)少なくとも1つの揮発性化合物を含有する流体(F)からの揮発性化合物の除去を含み、ここで、a.)流体(F)を少なくとも1つの対話装置で処理する工程と、b.)工程a.)からの濃縮流体を少なくとも1つの再処理装置で再処理する工程と、c.)工程b.)からの再処理された濃縮流体を少なくとも1つの再処理装置に供給する工程とを少なくとも含む方法により、上記した課題を解決する。
【選択図】図1
80 および溶媒を含まないポリマーの製造方法 JP2013500498 2011-03-23 JP5855083B2 2016-02-09 ポール・ヴァグナー; ハンス−インゴルフ・ポール; ロルフ・フェルラー; ヴォルフガング・クルンベ; アリシア・レ−サットラー; ハイケ・クロッペンブルク; マルティン・シェバーガー; ジョン・ラヴグローヴ
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