AU2001252301A1 - A method and an apparatus for preparing polyaniline - Google Patents
A method and an apparatus for preparing polyanilineInfo
- Publication number
- AU2001252301A1 AU2001252301A1 AU2001252301A AU5230101A AU2001252301A1 AU 2001252301 A1 AU2001252301 A1 AU 2001252301A1 AU 2001252301 A AU2001252301 A AU 2001252301A AU 5230101 A AU5230101 A AU 5230101A AU 2001252301 A1 AU2001252301 A1 AU 2001252301A1
- Authority
- AU
- Australia
- Prior art keywords
- reactor
- polymerization
- preparing polyaniline
- aniline
- oxidant
- 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.)
- Abandoned
Links
- 238000000034 method Methods 0.000 title abstract 2
- 229920000767 polyaniline Polymers 0.000 title abstract 2
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N Aniline Chemical compound NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 abstract 6
- 238000006116 polymerization reaction Methods 0.000 abstract 3
- 239000007800 oxidant agent Substances 0.000 abstract 2
- 230000001590 oxidative effect Effects 0.000 abstract 2
- 238000006243 chemical reaction Methods 0.000 abstract 1
- 230000003068 static effect Effects 0.000 abstract 1
Classifications
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1862—Stationary reactors having moving elements inside placed in series
-
- 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/18—Stationary reactors having moving elements inside
- B01J19/1868—Stationary reactors having moving elements inside resulting in a loop-type movement
- B01J19/1881—Stationary reactors having moving elements inside resulting in a loop-type movement externally, i.e. the mixture leaving the vessel and subsequently re-entering it
-
- 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
- C08G73/00—Macromolecular compounds obtained by reactions forming a linkage containing nitrogen with or without oxygen or carbon in the main chain of the macromolecule, not provided for in groups C08G12/00 - C08G71/00
- C08G73/02—Polyamines
- C08G73/026—Wholly aromatic polyamines
- C08G73/0266—Polyanilines or derivatives thereof
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00094—Jackets
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
- B01J2219/00103—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor in a heat exchanger separate from the reactor
-
- 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/00049—Controlling or regulating processes
- B01J2219/00051—Controlling the temperature
- B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
- B01J2219/00105—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling
- B01J2219/0011—Controlling the temperature by indirect heating or cooling employing heat exchange fluids part or all of the reactants being heated or cooled outside the reactor while recycling involving reactant liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Macromolecular Compounds Obtained By Forming Nitrogen-Containing Linkages In General (AREA)
- Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
Abstract
In a method for preparing polyaniline, aniline is polymerized in a reactor in a polymerization medium containing aniline and oxidant. The polymerization is performed in a reactor in which the ratio of the heat transfer surface to the reaction volume is at least 10/m, preferably at least 20/m. In the apparatus, the polymerization is performed in a tubular reactor (2) by allowing a medium containing aniline and oxidant to flow in a mixed flow through the tubular reactor. The tubular reactor is equipped with static mixers (4). There can be several tubular reactors (2) in parallel.
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI20000794 | 2000-04-04 | ||
| FI20000794A FI113053B (en) | 2000-04-04 | 2000-04-04 | A process for preparing polyaniline |
| US09/709,868 US6509502B1 (en) | 2000-04-04 | 2000-11-10 | Method and apparatus for preparing polyaniline |
| US09709868 | 2000-11-10 | ||
| PCT/FI2001/000330 WO2001074926A1 (en) | 2000-04-04 | 2001-04-04 | A method and an apparatus for preparing polyaniline |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AU2001252301A1 true AU2001252301A1 (en) | 2001-10-15 |
Family
ID=26160984
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| AU2001252301A Abandoned AU2001252301A1 (en) | 2000-04-04 | 2001-04-04 | A method and an apparatus for preparing polyaniline |
Country Status (8)
| Country | Link |
|---|---|
| EP (1) | EP1272546B1 (en) |
| JP (1) | JP4658436B2 (en) |
| CN (1) | CN1205253C (en) |
| AT (1) | ATE335037T1 (en) |
| AU (1) | AU2001252301A1 (en) |
| DE (1) | DE60121929T2 (en) |
| ES (1) | ES2269381T3 (en) |
| WO (1) | WO2001074926A1 (en) |
Families Citing this family (20)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100448916C (en) * | 2005-09-16 | 2009-01-07 | 西北师范大学 | A kind of water-soluble polyaniline high temperature resistant conductive material and preparation method thereof |
| CN1332997C (en) * | 2006-03-02 | 2007-08-22 | 扬州大学 | Chemical synthesization of poly-o-toluidine |
| CN100412109C (en) * | 2006-07-18 | 2008-08-20 | 重庆金固特化工新材料技术有限公司 | A synthetic device for industrial production of polyaniline |
| JP4911509B2 (en) * | 2007-04-03 | 2012-04-04 | 三洋電機株式会社 | Electrolytic capacitor and manufacturing method thereof |
| FR2928646B1 (en) * | 2008-03-13 | 2012-04-27 | Centre Nat Rech Scient | PROCESS FOR THE PREPARATION OF POLYANILINE AND HIGHLY SELF-ORIENTED FILMS OBTAINED |
| CN104231263B (en) * | 2013-06-19 | 2016-09-07 | 中国石油化工股份有限公司 | A kind of multistage continuous polyaniline synthesis technique |
| CN103408754B (en) * | 2013-07-11 | 2015-10-28 | 东华大学 | A kind of preparation method of polyaniline nano fiber |
| CN103408680A (en) * | 2013-08-27 | 2013-11-27 | 北京化工大学 | Energy-saving and high-efficiency self-cleaning polymerization process |
| US9481764B1 (en) * | 2015-10-13 | 2016-11-01 | The Boeing Company | Flow reactor synthesis of polymers |
| AU2016374658B2 (en) | 2015-12-23 | 2022-03-31 | Commonwealth Scientific And Industrial Research Organisation | A rotary device |
| US12343693B2 (en) | 2015-12-23 | 2025-07-01 | Commonwealth Scientific And Industrial Research Organisation | Static mixers for continuous flow catalytic reactors |
| CN105504278B (en) * | 2016-03-01 | 2017-08-04 | 扬州大学 | A kind of method of synthesizing polypyrrole |
| CN112020529A (en) | 2017-12-12 | 2020-12-01 | 波音公司 | Continuous flow method for preparing conductive polymers |
| US11248089B2 (en) * | 2019-04-10 | 2022-02-15 | The Boeing Company | Polyanilines and methods thereof |
| US11987669B2 (en) * | 2020-10-08 | 2024-05-21 | The Boeing Company | Polyaniline compositions, articles thereof, and methods thereof |
| US12448526B2 (en) | 2020-10-08 | 2025-10-21 | The Boeing Company | Conjugated polymer compositions, articles thereof, and methods thereof |
| CN112645290B (en) * | 2020-12-24 | 2022-12-09 | 河北纳泰化工有限公司 | Continuous production system and production method of potassium monopersulfate composite salt |
| CN112645859A (en) * | 2020-12-30 | 2021-04-13 | 山东尚舜化工有限公司 | Novel method and equipment for improving dispersity of promoter TMTD |
| CN113578229A (en) * | 2021-06-29 | 2021-11-02 | 浙江中科玖源新材料有限公司 | Polymerization reaction system capable of preventing violent heat release |
| CN116554467B (en) * | 2023-02-28 | 2025-09-23 | 常州大学 | A rapid self-polymerization polyaniline buffer and a rapid self-polymerization method |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS512788A (en) * | 1974-06-27 | 1976-01-10 | Mitsubishi Rayon Co | Jugonetsuno jokyoho |
| US5278240A (en) * | 1989-12-13 | 1994-01-11 | Exxon Chemical Patents Inc. | Oil soluble amino-substituted polymers containing graft polymer segments derived from aromatic nitrogen-containing monomers |
| US5276112A (en) * | 1991-11-07 | 1994-01-04 | Trustees Of The University Of Pennsylvania | High molecular weight polyanilines and synthetic methods therefor |
| FI93021C (en) * | 1992-12-31 | 1995-02-10 | Neste Oy | Process for polymerizing aniline by gradually adding aniline and oxidant |
| NZ279887A (en) * | 1994-03-04 | 1996-12-20 | Bicc Plc | Linear polyanilines;absence of chain branching indicated by < characterised by an nmr spectrum in its leuco form; method of making polyanilines and conductive, oriented film of such polymer |
| WO1998005043A1 (en) * | 1996-07-25 | 1998-02-05 | International Business Machines Corporation | Vibrational methods of deaggregation of electrically conductive polymers and precursors thereof |
| US6072027A (en) * | 1997-11-18 | 2000-06-06 | The Dow Chemical Company | Process for preparing an electrically conductive polymer |
| US5959072A (en) * | 1998-01-26 | 1999-09-28 | Conpoly Technology Co., Ltd. | Wastewater-recyclable process for producing a polyaniline resin powder |
| US6165418A (en) * | 1998-06-29 | 2000-12-26 | Mobil Oil Corporation | System for controlling temperature of a continuous polymerization process |
-
2001
- 2001-04-04 EP EP01925601A patent/EP1272546B1/en not_active Expired - Lifetime
- 2001-04-04 JP JP2001572609A patent/JP4658436B2/en not_active Expired - Fee Related
- 2001-04-04 WO PCT/FI2001/000330 patent/WO2001074926A1/en not_active Ceased
- 2001-04-04 CN CN01810595.5A patent/CN1205253C/en not_active Expired - Fee Related
- 2001-04-04 DE DE60121929T patent/DE60121929T2/en not_active Expired - Fee Related
- 2001-04-04 AT AT01925601T patent/ATE335037T1/en not_active IP Right Cessation
- 2001-04-04 AU AU2001252301A patent/AU2001252301A1/en not_active Abandoned
- 2001-04-04 ES ES01925601T patent/ES2269381T3/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| CN1205253C (en) | 2005-06-08 |
| ATE335037T1 (en) | 2006-08-15 |
| ES2269381T3 (en) | 2007-04-01 |
| CN1432033A (en) | 2003-07-23 |
| DE60121929T2 (en) | 2007-09-06 |
| JP2003529651A (en) | 2003-10-07 |
| EP1272546B1 (en) | 2006-08-02 |
| EP1272546A1 (en) | 2003-01-08 |
| DE60121929D1 (en) | 2006-09-14 |
| WO2001074926A1 (en) | 2001-10-11 |
| JP4658436B2 (en) | 2011-03-23 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| AU2001252301A1 (en) | A method and an apparatus for preparing polyaniline | |
| HUT59620A (en) | Apparatus and method for producing ethylene polymer | |
| DK1036100T3 (en) | Process for Preparing Ethylene Copolymers in Segmented Tube Reactors and Using the Copy Lymers as Fluid Enhancers | |
| MXPA05002958A (en) | Polymerization reactior having large length/diameter ratio. | |
| JPS6470507A (en) | Continuous bulk polymerization of styrene polymer | |
| Coelhoso et al. | Biofilm reactors: an experimental and modeling study of wastewater denitrification in fluidized‐bed reactors of activated carbon particles | |
| EG21081A (en) | Process for the gas phase polymerization of alpha - olefins | |
| AU2003293840A1 (en) | Method for the production of chlorine by means of gas phase oxidation of hydrogen chloride | |
| EP0985446A3 (en) | Two stage reactor for continuous three phase slurry hydrogenation and method of operation | |
| MY117027A (en) | Polymerization process using separated flow. | |
| AU1959592A (en) | Polymerisation reactor and polymerisation process | |
| JPS5655410A (en) | Continuous bulk polymerization of styrene type copolymer | |
| JPS55139471A (en) | Ink jet-registering ink composition | |
| EP0995489A3 (en) | Process for accelerating fast reactions using high intensity plug flow tubular reactors | |
| JPS57105410A (en) | Continuous preparation of polyvinyl acetate and polyvinyl alcohol having low polymerization degree | |
| CA2358970A1 (en) | Biochemically enhanced thermophilic treatment process | |
| JPS5641210A (en) | Preparation of vinyl chloride polymer | |
| JPS5633093A (en) | Anaerobic fermentation method | |
| JPS5798513A (en) | Production of hydrogel | |
| JPS54133584A (en) | Preparation of highly crystalline olefin polymer | |
| Chaudhry et al. | Modelling of simultaneous methanogenesis and denitrification in an upflow packed‐bed biofilm reactor | |
| AU4255796A (en) | Method of producing emulsion polymers | |
| EP0440997A3 (en) | Process for the preparation of polyketone polymers | |
| WO2001089683A3 (en) | Device and method for carrying out heterogeneously catalysed gas phase reactions with heat tonality | |
| JPS5693722A (en) | Production of nonaqueous polymer dispersion |