JP2958673B2 - アクリル酸の精製方法と装置、およびその方法により精製されたアクリル酸 - Google Patents
アクリル酸の精製方法と装置、およびその方法により精製されたアクリル酸Info
- Publication number
- JP2958673B2 JP2958673B2 JP6077928A JP7792894A JP2958673B2 JP 2958673 B2 JP2958673 B2 JP 2958673B2 JP 6077928 A JP6077928 A JP 6077928A JP 7792894 A JP7792894 A JP 7792894A JP 2958673 B2 JP2958673 B2 JP 2958673B2
- Authority
- JP
- Japan
- Prior art keywords
- acrylic acid
- crystallization
- static
- purification
- crystallizer
- 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 - Lifetime
Links
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 title claims description 86
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 title claims description 85
- 238000000034 method Methods 0.000 title claims description 43
- 239000013078 crystal Substances 0.000 claims description 93
- 230000003068 static effect Effects 0.000 claims description 62
- 238000000746 purification Methods 0.000 claims description 52
- 238000002425 crystallisation Methods 0.000 claims description 42
- 230000008025 crystallization Effects 0.000 claims description 41
- 238000001816 cooling Methods 0.000 claims description 20
- 238000001640 fractional crystallisation Methods 0.000 claims description 12
- 239000002178 crystalline material Substances 0.000 claims description 11
- 239000000725 suspension Substances 0.000 claims description 11
- 239000011552 falling film Substances 0.000 claims description 9
- 238000004090 dissolution Methods 0.000 claims description 8
- 238000003860 storage Methods 0.000 claims description 4
- 238000012432 intermediate storage Methods 0.000 claims 2
- 239000000061 acid fraction Substances 0.000 claims 1
- 238000005266 casting Methods 0.000 claims 1
- 239000012535 impurity Substances 0.000 description 32
- 239000000047 product Substances 0.000 description 30
- 239000000463 material Substances 0.000 description 21
- 239000006166 lysate Substances 0.000 description 13
- 238000010438 heat treatment Methods 0.000 description 12
- 239000000203 mixture Substances 0.000 description 10
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 8
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 6
- QQONPFPTGQHPMA-UHFFFAOYSA-N Propene Chemical compound CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 6
- 230000003647 oxidation Effects 0.000 description 6
- 238000007254 oxidation reaction Methods 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 238000004821 distillation Methods 0.000 description 5
- 239000000155 melt Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- HGINCPLSRVDWNT-UHFFFAOYSA-N Acrolein Chemical compound C=CC=O HGINCPLSRVDWNT-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 235000019260 propionic acid Nutrition 0.000 description 4
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 230000003197 catalytic effect Effects 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000012452 mother liquor Substances 0.000 description 3
- WJFKNYWRSNBZNX-UHFFFAOYSA-N 10H-phenothiazine Chemical compound C1=CC=C2NC3=CC=CC=C3SC2=C1 WJFKNYWRSNBZNX-UHFFFAOYSA-N 0.000 description 2
- 150000001299 aldehydes Chemical class 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000000539 dimer Substances 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000005496 eutectics Effects 0.000 description 2
- 229950000688 phenothiazine Drugs 0.000 description 2
- 239000012264 purified product Substances 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- 125000005396 acrylic acid ester group Chemical group 0.000 description 1
- 150000001253 acrylic acids Chemical class 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 150000001735 carboxylic acids Chemical class 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 238000005345 coagulation Methods 0.000 description 1
- 230000015271 coagulation Effects 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001548 drop coating Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- ZDGGJQMSELMHLK-UHFFFAOYSA-N m-Trifluoromethylhippuric acid Chemical compound OC(=O)CNC(=O)C1=CC=CC(C(F)(F)F)=C1 ZDGGJQMSELMHLK-UHFFFAOYSA-N 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- -1 surface coatings Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0004—Crystallisation cooling by heat exchange
- B01D9/0013—Crystallisation cooling by heat exchange by indirect heat exchange
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/004—Fractional crystallisation; Fractionating or rectifying columns
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0059—General arrangements of crystallisation plant, e.g. flow sheets
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/43—Separation; Purification; Stabilisation; Use of additives by change of the physical state, e.g. crystallisation
Landscapes
- Chemical & Material Sciences (AREA)
- Crystallography & Structural Chemistry (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH00922/93-8 | 1993-03-26 | ||
| CH92293 | 1993-03-26 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH0748311A JPH0748311A (ja) | 1995-02-21 |
| JP2958673B2 true JP2958673B2 (ja) | 1999-10-06 |
Family
ID=4198293
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP6077928A Expired - Lifetime JP2958673B2 (ja) | 1993-03-26 | 1994-03-25 | アクリル酸の精製方法と装置、およびその方法により精製されたアクリル酸 |
Country Status (9)
| Country | Link |
|---|---|
| US (1) | US5504247A (enExample) |
| EP (1) | EP0616998B1 (enExample) |
| JP (1) | JP2958673B2 (enExample) |
| KR (1) | KR100219943B1 (enExample) |
| CN (1) | CN1058256C (enExample) |
| DE (1) | DE59400240D1 (enExample) |
| ES (1) | ES2086990T3 (enExample) |
| SG (1) | SG93785A1 (enExample) |
| TW (1) | TW305830B (enExample) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007191449A (ja) * | 2006-01-20 | 2007-08-02 | Nippon Shokubai Co Ltd | アクリル酸の製造方法 |
| JP2011213735A (ja) * | 2011-07-19 | 2011-10-27 | Nippon Shokubai Co Ltd | アクリル酸の製造方法 |
Families Citing this family (96)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2727061B2 (ja) | 1993-10-13 | 1998-03-11 | 日揮株式会社 | 晶析方法及び晶析装置 |
| JP3724864B2 (ja) * | 1995-12-01 | 2005-12-07 | 日揮株式会社 | 晶析方法 |
| DE19600955A1 (de) * | 1996-01-12 | 1997-07-17 | Basf Ag | Verfahren zur Herstellung von Acrylsäure und deren Ester |
| DE19606877A1 (de) * | 1996-02-23 | 1997-08-28 | Basf Ag | Verfahren zur Reinigung von Acrylsäure und Methacrylsäure |
| DE19627847A1 (de) * | 1996-07-10 | 1998-01-15 | Basf Ag | Verfahren zur Herstellung von Acrylsäure |
| DE19627679A1 (de) * | 1996-07-10 | 1998-01-15 | Basf Ag | Verfahren zur Reinigung von Roh-Acrylsäure durch Kristallisation |
| GB9714632D0 (en) * | 1997-07-12 | 1997-09-17 | Ici Plc | Process for the production of methyl methacrylate |
| MY120051A (en) * | 1997-07-30 | 2005-08-30 | Mitsubishi Rayon Co | Process for purification of (meth)acrylic acid |
| DE19740252A1 (de) | 1997-09-12 | 1999-03-18 | Basf Ag | Verfahren zur Herstellung von Acrylsäure und Methacrylsäure |
| DE19829477A1 (de) * | 1998-07-01 | 2000-01-05 | Basf Ag | Verfahren zur Reinigung von Acrylsäure oder Methacrylsäure durch Kristallisation und Destillation |
| DE19833049A1 (de) * | 1998-07-22 | 2000-01-27 | Basf Ag | Verfahren zur Herstellung von Acrylsäure |
| DE19904820A1 (de) * | 1999-02-05 | 2000-08-10 | Stockhausen Chem Fab Gmbh | Verfahren und Vorrichtung zur Reinigung von Stoffen mittels Kristallisation |
| MY122671A (en) | 1999-03-06 | 2006-04-29 | Basf Ag | Fractional condensation of a product gas mixture containing acrylic acid |
| DE19923389A1 (de) | 1999-05-21 | 2000-08-17 | Basf Ag | Verfahren zum Lagern und/oder Transportieren von Reinacrylsäure |
| US6500982B1 (en) * | 1999-06-28 | 2002-12-31 | Rohm And Haas Company | Process for preparing (meth) acrylic acid |
| AU7489300A (en) * | 1999-09-22 | 2001-04-24 | Cognis Corporation | Purification and recovery of dicarboxylic acids using melt crystallization |
| FR2799386B1 (fr) * | 1999-10-12 | 2001-12-28 | Befs Prokem | Procede de purification de produits organiques par cristallisation fractionnee a vitesse de circulation variable |
| JP3938646B2 (ja) | 2000-01-14 | 2007-06-27 | 株式会社日本触媒 | アクリル酸の製造方法 |
| DE10003498A1 (de) * | 2000-01-27 | 2001-08-02 | Basf Ag | Reinigungsverfahren für (Meth)acrylsäure |
| JP4960562B2 (ja) * | 2000-04-11 | 2012-06-27 | ビーエーエスエフ ソシエタス・ヨーロピア | 粗製アクリル酸溶融物の精製法 |
| DE10026407A1 (de) | 2000-05-29 | 2001-12-06 | Basf Ag | Verfahren der diskontinuierlichen kristallisativen Reinigung von Roh-Acrylsäure |
| JP4673958B2 (ja) * | 2000-06-19 | 2011-04-20 | 株式会社日本触媒 | 固形物除去装置 |
| JP5008215B2 (ja) * | 2000-09-29 | 2012-08-22 | 三菱瓦斯化学株式会社 | 晶析方法および装置 |
| EP1349826B1 (de) | 2001-01-12 | 2012-06-27 | Evonik Stockhausen GmbH | Kontinuierliches verfahren zur herstellung und aufreinigung von (meth) acrylsäure |
| DE10122787A1 (de) | 2001-05-10 | 2002-06-06 | Basf Ag | Verfahren zur Herstellung einer gereinigten Schmelze wenigstens eines Monomeren |
| DE10122788A1 (de) | 2001-05-10 | 2002-06-06 | Basf Ag | Verfahren der kristallisativen Reinigung einer Roh-Schmelze wenigstens eines Monomeren |
| ES2387564T3 (es) * | 2001-12-04 | 2012-09-26 | Mitsubishi Chemical Corporation | Procedimiento de producción de compuestos de ácido (met)acrílico |
| DE10211686A1 (de) | 2002-03-15 | 2003-10-02 | Stockhausen Chem Fab Gmbh | (Meth)Acrylsäurekristall und Verfahren zur Herstellung und Aufreinigung von wässriger (Meth)Acrylsäure |
| DE10221176A1 (de) * | 2002-05-13 | 2003-11-27 | Basf Ag | Verfahren zur Herstellung geruchsarmer Hydrogelbildender Polymerisate |
| DE10301040B4 (de) | 2003-01-13 | 2005-07-21 | Stockhausen Gmbh | Aufreinigung eines Monomers durch Extraktion mit einem Phasenbildner und Kristallisation |
| JP2005247731A (ja) * | 2004-03-03 | 2005-09-15 | Mitsubishi Chemicals Corp | （メタ）アクリル酸組成物及びその製造方法 |
| DE102004034316B4 (de) * | 2004-07-15 | 2015-07-16 | Evonik Degussa Gmbh | Ein Verfahren zur Herstellung von (Meth)Acrylsäure |
| DE102004044639A1 (de) * | 2004-09-13 | 2006-05-24 | Stockhausen Gmbh | Verfahren zur extraktiven Aufreinigung von (Meth)Acrylsäure unter Einsatz eines Trennmittels |
| DE102004044638A1 (de) * | 2004-09-13 | 2006-03-30 | Stockhausen Gmbh | Aufreinigung eines (Meth)Acrylsäure enthaltenen Destillationssumpfprodukts durch Kristallisation |
| DE102004058907A1 (de) | 2004-12-07 | 2006-06-08 | Basf Ag | Reinigung von ionischen Flüssigkeiten |
| DE102005009890A1 (de) * | 2005-03-01 | 2006-09-07 | Basf Ag | Verfahren zur Abtrennung von Methacrylsäure aus Acrylsäure als Hauptbestandteil sowie Zielprodukt und Methacrylsäure als Nebenkomponente enthaltender flüssiger Phase |
| US7705181B2 (en) | 2005-03-01 | 2010-04-27 | Basf Akiengesellschaft | Process for removing methacrylic acid from liquid phase comprising acrylic acid as a main constituent and target product, and methacrylic acid as a secondary component |
| EP1856020B1 (de) * | 2005-03-01 | 2015-07-08 | Basf Se | Verfahren zur abtrennung von methacrylsäure aus acrylsäure als hauptbestandteil sowie zielprodukt und methacrylsäure als nebenkomponente enthaltender flüssiger phase |
| EP2066416B1 (de) | 2006-09-12 | 2011-08-31 | Sulzer Chemtech AG | Verfahren zur reinigung von ionischen flüssigkeiten |
| DE102007004960A1 (de) | 2007-01-26 | 2008-07-31 | Basf Se | Verfahren zur Herstellung von Acrylsäure |
| DE102007055086A1 (de) | 2007-11-16 | 2009-05-20 | Basf Se | Verfahren zur Herstellung von Acrylsäure |
| DE102007014606A1 (de) | 2007-03-23 | 2008-09-25 | Basf Se | Verfahren zur Lagerung einer unter den Bedingungen der Lagerung flüssigen Monomerenphase |
| DE102007014603A1 (de) | 2007-03-23 | 2008-09-25 | Basf Se | Verfahren des Transports einer aus einem Lagerbehälter entnommenen flüssigen Monomerenphase im Tank eines Tankwagens oder eines Tankschiffs |
| DE102007043748A1 (de) * | 2007-09-13 | 2008-09-11 | Basf Se | Verfahren zur kontinuierlichen Abtrennung eines Zielproduktes X in Form von feinteiligem Kristallisat |
| JP4822559B2 (ja) * | 2007-09-19 | 2011-11-24 | ローム アンド ハース カンパニー | （メタ）アクリル酸生成物流からのプロピオン酸の選択的減少のための改良された方法 |
| EP2085376B1 (en) | 2008-01-30 | 2012-09-05 | Evonik Röhm GmbH | Process for preparation of high purity methacrylic acid |
| FR2934264B1 (fr) * | 2008-07-22 | 2012-07-20 | Arkema France | Fabrication d'esters de vinyle a partir de matieres renouvelables, esters de vinyle obtenus et utilisations |
| DE102008040799A1 (de) | 2008-07-28 | 2008-12-11 | Basf Se | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enthaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal |
| DE102008041573A1 (de) | 2008-08-26 | 2010-03-04 | Basf Se | Verfahren zur Auftrennung von in einem Produktgasgemisch einer partiellen heterogen katalysierten Gasphasenoxidation einer C3-Vorläuferverbindung der Acrylsäure als Hauptbestandteil enhaltener Acrylsäure und als Nebenprodukt enthaltenem Glyoxal |
| MY153094A (en) | 2008-07-28 | 2014-12-31 | Basf Se | Process for separating acrylic acid present as a main constituent and glyoxal present as a by-product in a product gas mixture of a partial heterogeneously catalyzed gas phase oxidation of a c3 precursor compound of acrylic acid |
| WO2010134434A1 (ja) * | 2009-05-19 | 2010-11-25 | 株式会社日本触媒 | (メタ)アクリル酸の製造方法 |
| JP5583666B2 (ja) * | 2009-06-01 | 2014-09-03 | 株式会社日本触媒 | （メタ）アクリル酸の晶析方法および製品（メタ）アクリル酸の重合防止剤含有量の調整方法 |
| CN102471214B (zh) * | 2009-06-30 | 2014-10-01 | 株式会社日本触媒 | 丙烯酸的析晶装置及使用其的丙烯酸的析晶方法 |
| CN102471212B (zh) * | 2009-07-01 | 2014-09-17 | 株式会社日本触媒 | (甲基)丙烯酸的制备方法 |
| JP5830378B2 (ja) * | 2009-07-02 | 2015-12-09 | 株式会社日本触媒 | （メタ）アクリル酸の製造方法 |
| CN102471213B (zh) * | 2009-07-03 | 2014-06-04 | 株式会社日本触媒 | (甲基)丙烯酸的结晶装置和(甲基)丙烯酸的结晶方法 |
| FR2948366B1 (fr) | 2009-07-22 | 2012-08-17 | Arkema France | Procede de fabrication d'acide acrylique bio-ressource a partir de glycerol |
| FR2948365B1 (fr) * | 2009-07-22 | 2011-09-09 | Arkema France | Procede de fabrication d'acide acrylique bio-ressource a partir de glycerol |
| DE102010031507A1 (de) | 2010-06-02 | 2011-12-08 | Evonik Stockhausen Gmbh | Verfahren zur Reinigung kristalliner Phasen aus Produktgemischen mittels Schichtkristallisation |
| DE102011076931A1 (de) | 2011-06-03 | 2012-12-06 | Basf Se | Wässrige Lösung, enthaltend Acrylsäure und deren konjugierte Base |
| US8658822B2 (en) | 2011-10-03 | 2014-02-25 | Celanese International Corporation | Processes for producing acrylic acids and acrylates |
| US8536368B2 (en) | 2011-10-03 | 2013-09-17 | Celanese International Corporation | Processes for the production of acrylic acids and acrylates from a trioxane feed |
| US8729299B2 (en) | 2011-10-03 | 2014-05-20 | Celanese International Corporation | Processes for the production of acrylic acids and acrylates |
| WO2013163806A1 (en) | 2012-05-03 | 2013-11-07 | Evonik Industries Ag | Process for preparation of highly pure, non-yellowing methacrylic acid |
| JP6134811B2 (ja) * | 2013-01-14 | 2017-05-24 | スルザー ケムテック アクチェンゲゼルシャフト | 化合物を精製するための多段階晶析方法及び装置 |
| EP2777791A1 (en) | 2013-03-11 | 2014-09-17 | Sulzer Chemtech AG | Process and apparatus for purification of a stream containing a cyclic ester of an alpha-hydroxycarboxylic acid |
| JP2016516732A (ja) | 2013-03-18 | 2016-06-09 | エボニック レーム ゲゼルシャフト ミット ベシュレンクテル ハフツングＥｖｏｎｉｋ Ｒｏｅｈｍ ＧｍｂＨ | メタクリル酸及びメタクリル酸エステルの製造方法 |
| US9073846B2 (en) | 2013-06-05 | 2015-07-07 | Celanese International Corporation | Integrated process for the production of acrylic acids and acrylates |
| US9120743B2 (en) | 2013-06-27 | 2015-09-01 | Celanese International Corporation | Integrated process for the production of acrylic acids and acrylates |
| WO2015036273A1 (de) | 2013-09-12 | 2015-03-19 | Basf Se | Verfahren zur herstellung von acrylsäure |
| EP3145965B1 (de) * | 2014-05-19 | 2020-02-19 | Basf Se | Verfahren zur kontinuierlichen dehydratisierung von 3-hydroxypropionsäure zu acrylsäure |
| WO2016026763A1 (en) | 2014-08-18 | 2016-02-25 | Basf Se | Process for preparing acrylic acid using a heterogeneous alumina catalyst |
| EP3012244A1 (en) | 2014-10-24 | 2016-04-27 | Sulzer Chemtech AG | Process and apparatus for purification of acrylic acid |
| DE102014017804A1 (de) | 2014-12-02 | 2016-04-21 | Basf Se | Verfahren zur Herstellung von Acrylsäure |
| WO2016135020A1 (de) | 2015-02-24 | 2016-09-01 | Basf Se | Verfahren zur kontinuierlichen dehydratisierung von 3-hydroxypropionsäure zu acrylsäure |
| WO2016162175A1 (de) | 2015-04-07 | 2016-10-13 | Basf Se | Verfahren zur dehydratisierung von 3-hydroxypropionsäure zu acrylsäure |
| EP3103539A1 (en) * | 2015-06-11 | 2016-12-14 | Sulzer Chemtech AG | Method and apparatus for purifying a mixture comprising oil and wax |
| FR3041958B1 (fr) | 2015-10-06 | 2019-06-14 | Arkema France | Procede ameliore de production d’acide (meth)acrylique de grade polymere |
| ES2667205T3 (es) * | 2015-11-30 | 2018-05-10 | Evonik Degussa Gmbh | Depuración fina de isoforonanitrilo mediante cristalización por fusión |
| WO2017122040A1 (en) | 2016-01-12 | 2017-07-20 | Sabic Global Technologies B.V. | A dynamic melt crystallization process for purifying dicyclopentadiene from a mixed liquid hydrocarbon stream |
| US10968160B2 (en) | 2016-12-22 | 2021-04-06 | Eastman Chemical Company | Separation of propionic acid from acrylic acid via azeotropic distillation |
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| CN108707072A (zh) * | 2018-05-10 | 2018-10-26 | 宜兴丹森科技有限公司 | 丙烯酸组合物的纯化方法 |
| FR3094716B1 (fr) | 2019-04-02 | 2021-06-04 | Arkema France | Production d’acide acrylique de grade polymere |
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| FR3108906B1 (fr) | 2020-04-06 | 2022-03-04 | Arkema France | Procede de purification d’acide (meth)acrylique |
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| CN113144660B (zh) * | 2021-02-05 | 2023-03-03 | 成都思达能环保设备有限公司 | 一种结晶方法及系统 |
| WO2023006503A1 (de) | 2021-07-28 | 2023-02-02 | Basf Se | Verfahren zur herstellung von acrylsäure |
| WO2025078224A1 (de) | 2023-10-11 | 2025-04-17 | Basf Se | Verfahren zur aufreinigung von acrylsäure durch kreisgasrückführung |
| WO2025078225A1 (de) | 2023-10-11 | 2025-04-17 | Basf Se | Verfahren zur aufreinigung von acrylsäure durch muttersäurerückführung |
| WO2025172146A1 (de) | 2024-02-15 | 2025-08-21 | Basf Se | Verfahren zur herstellung von acrylsäure |
| WO2025219137A1 (en) | 2024-04-17 | 2025-10-23 | Basf Se | Process for utilizing acrylic acid production waste streams by gasification and fermentation |
| WO2025219136A1 (en) | 2024-04-17 | 2025-10-23 | Basf Se | Process for utilizing acrylic acid production waste streams |
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Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| BE521274A (enExample) * | 1952-07-11 | |||
| US2885431A (en) * | 1954-06-21 | 1959-05-05 | Phillips Petroleum Co | Separation by crystallization |
| US2868830A (en) * | 1954-10-18 | 1959-01-13 | Phillips Petroleum Co | Separation by crystallization |
| US3050952A (en) * | 1960-10-05 | 1962-08-28 | Phillips Petroleum Co | Separation by crystallization |
| DE1620756A1 (de) * | 1966-07-13 | 1970-07-16 | Vickers Zimmer Ag Plangung Und | Verfahren zur Reinigung von stark verunreinigten Lactamen von omega-Aminocarbonsaeuren |
| AT279547B (de) * | 1967-04-14 | 1970-03-10 | Buchs Metallwerk Ag | Verfahren und Vorrichtung zur Trennung oder Reinigung schmelzflüssiger, flüssiger oder gelöster Stoffe durch fraktioniertes Kristallisieren |
| DE2606364C3 (de) * | 1976-02-18 | 1988-05-26 | Basf Ag, 6700 Ludwigshafen | Verfahren zur Stofftrennung aus einem flüssigen Gemisch durch fraktionierte Kristallisation |
| US4230888A (en) * | 1977-12-15 | 1980-10-28 | Standard Oil Company (Ohio) | Process for purification of acrylic acid by fractional crystallization |
| US4780568A (en) * | 1984-12-14 | 1988-10-25 | Ashland Oil, Inc. | Purification of methacrylic acid from an oxydehydrogenation by crystallization |
-
1994
- 1994-03-08 TW TW083101994A patent/TW305830B/zh not_active IP Right Cessation
- 1994-03-14 DE DE59400240T patent/DE59400240D1/de not_active Expired - Lifetime
- 1994-03-14 SG SG9606214A patent/SG93785A1/en unknown
- 1994-03-14 EP EP94810158A patent/EP0616998B1/de not_active Expired - Lifetime
- 1994-03-14 ES ES94810158T patent/ES2086990T3/es not_active Expired - Lifetime
- 1994-03-22 US US08/216,162 patent/US5504247A/en not_active Expired - Lifetime
- 1994-03-24 KR KR1019940005927A patent/KR100219943B1/ko not_active Expired - Lifetime
- 1994-03-25 JP JP6077928A patent/JP2958673B2/ja not_active Expired - Lifetime
- 1994-03-26 CN CN94103445A patent/CN1058256C/zh not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007191449A (ja) * | 2006-01-20 | 2007-08-02 | Nippon Shokubai Co Ltd | アクリル酸の製造方法 |
| JP2011213735A (ja) * | 2011-07-19 | 2011-10-27 | Nippon Shokubai Co Ltd | アクリル酸の製造方法 |
Also Published As
| Publication number | Publication date |
|---|---|
| EP0616998A1 (de) | 1994-09-28 |
| JPH0748311A (ja) | 1995-02-21 |
| CN1105014A (zh) | 1995-07-12 |
| KR100219943B1 (ko) | 1999-09-01 |
| EP0616998B1 (de) | 1996-05-01 |
| DE59400240D1 (de) | 1996-06-05 |
| TW305830B (enExample) | 1997-05-21 |
| SG93785A1 (en) | 2003-01-21 |
| CN1058256C (zh) | 2000-11-08 |
| ES2086990T3 (es) | 1996-07-01 |
| US5504247A (en) | 1996-04-02 |
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