RU2008135966A - Способ получения акриловой кислоты - Google Patents
Способ получения акриловой кислоты Download PDFInfo
- Publication number
- RU2008135966A RU2008135966A RU2008135966/04A RU2008135966A RU2008135966A RU 2008135966 A RU2008135966 A RU 2008135966A RU 2008135966/04 A RU2008135966/04 A RU 2008135966/04A RU 2008135966 A RU2008135966 A RU 2008135966A RU 2008135966 A RU2008135966 A RU 2008135966A
- Authority
- RU
- Russia
- Prior art keywords
- propylene
- acrylic acid
- oxidation
- stage
- acrolein
- Prior art date
Links
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical compound OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 title claims abstract 7
- 238000004519 manufacturing process Methods 0.000 title abstract 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract 16
- HGINCPLSRVDWNT-UHFFFAOYSA-N Acrolein Chemical compound C=CC=O HGINCPLSRVDWNT-UHFFFAOYSA-N 0.000 claims abstract 12
- 238000000034 method Methods 0.000 claims abstract 10
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims abstract 10
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims abstract 10
- 230000003647 oxidation Effects 0.000 claims abstract 7
- 238000007254 oxidation reaction Methods 0.000 claims abstract 7
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims abstract 5
- 238000006297 dehydration reaction Methods 0.000 claims abstract 5
- 230000018044 dehydration Effects 0.000 claims abstract 4
- 239000007789 gas Substances 0.000 claims abstract 4
- 239000012495 reaction gas Substances 0.000 claims abstract 2
- 235000011187 glycerol Nutrition 0.000 claims 5
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims 2
- 229910001882 dioxygen Inorganic materials 0.000 claims 2
- 239000003054 catalyst Substances 0.000 claims 1
- 239000007788 liquid Substances 0.000 claims 1
- 239000002994 raw material Substances 0.000 abstract 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/51—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
- C07C45/52—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition by dehydration and rearrangement involving two hydroxy groups in the same molecule
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
- B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
- B01J8/0457—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being placed in separate reactors
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0492—Feeding reactive fluids
-
- 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
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
- B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
- B01J8/0496—Heating or cooling the reactor
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/27—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation
- C07C45/32—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen
- C07C45/33—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties
- C07C45/34—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds
- C07C45/35—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by oxidation with molecular oxygen of CHx-moieties in unsaturated compounds in propene or isobutene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/16—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation
- C07C51/21—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen
- C07C51/23—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups
- C07C51/235—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of oxygen-containing groups to carboxyl groups of —CHO groups or primary alcohol groups
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
- B01J2208/00106—Controlling the temperature by indirect heat exchange
- B01J2208/00168—Controlling the temperature by indirect heat exchange with heat exchange elements outside the bed of solid particles
- B01J2208/00203—Coils
-
- 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
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00796—Details of the reactor or of the particulate material
- B01J2208/00805—Details of the particulate material
- B01J2208/00814—Details of the particulate material the particulate material being provides in prefilled containers
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
1. Способ получения акриловой кислоты из пропилена, включающий первую стадию окисления пропилена до акролеина и вторую стадию окисления акролеина до акриловой кислоты, отличающийся тем, что он включает стадию дегидратации глицерина, осуществляемую в присутствии газа, содержащего пропилен. ! 2. Способ по п.1, отличающийся тем, что газ, содержащий пропилен, представляет собой реакционный газ, выходящий со стадии окисления пропилена до акролеина. ! 3. Способ по п.1 или 2, отличающийся тем, что реакцию дегидратации осуществляют в газовой фазе в присутствии катализатора. ! 4. Способ по п.1 или 2, отличающийся тем, что добавляют молекулярный кислород на стадии дегидратации глицерина. ! 5. Способ по п.3, отличающийся тем, что добавляют молекулярный кислород на стадии дегидратации глицерина. ! 6. Способ по п.1 или 2, отличающийся тем, что глицерин вводят в жидком или газообразном виде. ! 7. Способ по п.1 или 2, отличающийся тем, что используют глицерин в чистом виде, или в виде концентрированного или разбавленного раствора. ! 8. Способ по п.1 или 2, отличающийся тем, что окисление пропилена осуществляют в присутствии избытка тепла.
Claims (8)
1. Способ получения акриловой кислоты из пропилена, включающий первую стадию окисления пропилена до акролеина и вторую стадию окисления акролеина до акриловой кислоты, отличающийся тем, что он включает стадию дегидратации глицерина, осуществляемую в присутствии газа, содержащего пропилен.
2. Способ по п.1, отличающийся тем, что газ, содержащий пропилен, представляет собой реакционный газ, выходящий со стадии окисления пропилена до акролеина.
3. Способ по п.1 или 2, отличающийся тем, что реакцию дегидратации осуществляют в газовой фазе в присутствии катализатора.
4. Способ по п.1 или 2, отличающийся тем, что добавляют молекулярный кислород на стадии дегидратации глицерина.
5. Способ по п.3, отличающийся тем, что добавляют молекулярный кислород на стадии дегидратации глицерина.
6. Способ по п.1 или 2, отличающийся тем, что глицерин вводят в жидком или газообразном виде.
7. Способ по п.1 или 2, отличающийся тем, что используют глицерин в чистом виде, или в виде концентрированного или разбавленного раствора.
8. Способ по п.1 или 2, отличающийся тем, что окисление пропилена осуществляют в присутствии избытка тепла.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR0601061A FR2897059B1 (fr) | 2006-02-07 | 2006-02-07 | Procede de preparation d'acide acrylique |
| FR0601061 | 2006-02-07 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| RU2008135966A true RU2008135966A (ru) | 2010-03-20 |
| RU2397156C2 RU2397156C2 (ru) | 2010-08-20 |
Family
ID=37075914
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2008135966/04A RU2397156C2 (ru) | 2006-02-07 | 2007-02-06 | Способ получения акриловой кислоты |
Country Status (16)
| Country | Link |
|---|---|
| US (1) | US7880034B2 (ru) |
| EP (1) | EP1981835B1 (ru) |
| JP (1) | JP5097128B2 (ru) |
| KR (1) | KR101004593B1 (ru) |
| CN (1) | CN101400639B (ru) |
| AT (1) | ATE430724T1 (ru) |
| BR (1) | BRPI0707533A2 (ru) |
| DE (1) | DE602007001072D1 (ru) |
| ES (1) | ES2325695T3 (ru) |
| FR (1) | FR2897059B1 (ru) |
| MY (1) | MY139630A (ru) |
| PL (1) | PL1981835T3 (ru) |
| PT (1) | PT1981835E (ru) |
| RU (1) | RU2397156C2 (ru) |
| WO (1) | WO2007090991A2 (ru) |
| ZA (1) | ZA200806644B (ru) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2606623C2 (ru) * | 2010-09-16 | 2017-01-10 | Басф Се | Способ получения акриловой кислоты из этанола и формальдегида |
| RU2610431C2 (ru) * | 2010-09-16 | 2017-02-10 | Басф Се | Способ получения акриловой кислоты из метанола и уксусной кислоты |
Families Citing this family (26)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2920767B1 (fr) * | 2007-09-06 | 2009-12-18 | Arkema France | Procede de vaporisation reactive de glycerol |
| FR2934261B1 (fr) * | 2008-07-25 | 2015-04-10 | Arkema France | Procede de synthese d'esters de l'acide acrylique |
| JP2011529094A (ja) | 2008-07-28 | 2011-12-01 | ビーエーエスエフ ソシエタス・ヨーロピア | アクリル酸のc3前駆体化合物のガス状生成混合物から主生成物として含有されるアクリル酸および副生成物として含有されるグリオキサールを分離する方法 |
| 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 |
| 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 |
| JP5305827B2 (ja) * | 2008-10-17 | 2013-10-02 | 株式会社日本触媒 | アクロレイン及びアクリル酸の製造方法 |
| FR2943351B1 (fr) * | 2009-03-18 | 2011-04-29 | Arkema France | Agent de mise en oeuvre acrylique |
| US8105971B2 (en) * | 2009-04-02 | 2012-01-31 | Lummus Technology Inc. | Process for making catalysts useful for the conversion of paraffins to olefins |
| DE102010001228A1 (de) | 2010-01-26 | 2011-02-17 | Basf Se | Verfahren der Abtrennung von Acrylsäure aus dem Produktgasgemisch einer heterogen katalysierten partiellen Gasphasenoxidation wenigstens einer C3-Vorläuferverbindung |
| DE102009027401A1 (de) | 2009-07-01 | 2010-02-18 | Basf Se | Verfahren der Abtrennung von Acrylsäure aus dem Produktgasgemisch einer heterogen katalysierten partiellen Gasphasenoxidation wenigstens einer C3-Vorläuferverbindung |
| WO2011000808A2 (de) | 2009-07-01 | 2011-01-06 | Basf Se | Verfahren der abtrennung von acrylsäure aus dem produktgasgemisch einer heterogen katalysierten partiellen gasphasenoxidation wenigstens einer c3-vorläuferverbindung |
| FR2948365B1 (fr) * | 2009-07-22 | 2011-09-09 | Arkema France | Procede de fabrication d'acide acrylique bio-ressource a partir de glycerol |
| JP5784609B2 (ja) | 2009-09-18 | 2015-09-24 | 日本化薬株式会社 | グリセリンの脱水反応によってアクロレインおよび/またはアクリル酸を製造するための触媒および方法 |
| FR2958185B1 (fr) * | 2010-03-30 | 2012-04-20 | Arkema France | Procede d'oxydation selective de monoxyde de carbone |
| WO2012010923A1 (en) | 2010-07-19 | 2012-01-26 | Arkema France | Process for manufacturing acrolein from glycerol |
| DE102010042216A1 (de) | 2010-10-08 | 2011-06-09 | Basf Se | Verfahren zur Hemmung der unerwünschten radikalischen Polymerisation von in einer flüssigen Phase P befindlicher Acrylsäure |
| DE102011076931A1 (de) | 2011-06-03 | 2012-12-06 | Basf Se | Wässrige Lösung, enthaltend Acrylsäure und deren konjugierte Base |
| WO2013008279A1 (en) | 2011-07-14 | 2013-01-17 | Nippon Kayaku Kabushiki Kaisha | Process for preparing catalyst used in production of acrolein and/or acrylic acid and process for preparing acrolein and/or acrylic acid by dehydration reaction of glycerin |
| WO2013017904A1 (en) | 2011-07-29 | 2013-02-07 | Arkema France | Improved process of dehydration reactions |
| FR2989684B1 (fr) * | 2012-04-18 | 2014-10-31 | Arkema France | Procede de fabrication d'acroleine et/ou d'acide acrylique a partir de glycerol |
| US9440903B2 (en) | 2012-09-24 | 2016-09-13 | Arkema Inc. | Shell and tube oxidation reactor with improved resistance to fouling |
| WO2014195157A1 (de) * | 2013-06-03 | 2014-12-11 | Evonik Degussa Gmbh | Verfahren zur herstellung von acrolein |
| US9776940B2 (en) | 2015-08-07 | 2017-10-03 | Basf Se | Process for production of acrylic acid |
| KR102044428B1 (ko) | 2015-12-23 | 2019-12-02 | 주식회사 엘지화학 | 글리세린으로부터 아크릴산의 제조방법 |
| JP7384519B2 (ja) | 2018-07-26 | 2023-11-21 | ベーアーエスエフ・エスエー | 液相pに存在するアクリル酸の望ましくないラジカル重合を抑制するための方法 |
| JP7651589B2 (ja) | 2020-03-26 | 2025-03-26 | ベーアーエスエフ・エスエー | 液相pに存在するアクリル酸の望ましくないフリーラジカル重合を抑制する方法 |
Family Cites Families (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR695931A (fr) | 1929-06-15 | 1930-12-23 | Schering Kahlbaum Ag | Procédé de fabrication d'acroléine |
| US2558520A (en) * | 1948-01-29 | 1951-06-26 | Us Ind Chemicals Inc | Production of acrolein from glycerol |
| GB1152215A (en) * | 1965-10-12 | 1969-05-14 | Rohm & Haas | Preparation of Acrolein |
| JPS55102536A (en) * | 1979-01-30 | 1980-08-05 | Mitsubishi Petrochem Co Ltd | Preparation of acrylic acid |
| US5080898A (en) * | 1982-05-12 | 1992-01-14 | The University Hospital | Enzymatically active toxin coupled to a cell-specific ligand |
| CA1299193C (en) * | 1986-07-17 | 1992-04-21 | Gordon Gene Harkreader | Anhydrous diluents for the propylene oxidation reaction to acrolein and acrolein oxidation to acrylic acid |
| CA1305178C (en) * | 1986-08-21 | 1992-07-14 | Gordon Gene Harkreader | Anhydrous diluent process for the propylene oxidation reaction to acrolein and acrolein oxidation to acrylic acid |
| JPH0813777B2 (ja) * | 1986-12-11 | 1996-02-14 | 三菱化学株式会社 | アクリル酸の製造法 |
| AU606160B2 (en) * | 1987-05-27 | 1991-01-31 | Nippon Shokubai Kagaku Kogyo Co. Ltd. | Process for production of acrylic acid |
| JPH0686399B2 (ja) * | 1987-05-27 | 1994-11-02 | 株式会社日本触媒 | アクリル酸の製造方法 |
| US5218146A (en) * | 1987-05-27 | 1993-06-08 | Nippon Shokubai Kagaku Kogyo Co., Ltd. | Process for production of acrylic acid |
| DE4238493C1 (de) * | 1992-11-14 | 1994-04-21 | Degussa | Verfahren zur Herstellung von Acrolein und dessen Verwendung |
| TW476746B (en) | 1997-07-23 | 2002-02-21 | Shell Int Research | Hydrogenolysis of glycerol |
| DE19848208A1 (de) | 1998-10-20 | 2000-04-27 | Deg Engineering Gmbh | Reaktor für die katalytische Umsetzung von Reaktionsmedien, insbesondere von gasförmigen Reaktionsmedien |
| DE10019381B4 (de) | 2000-04-19 | 2006-05-18 | Daun, Klaus-Dieter, Dipl.-Ing. | Reaktor für die katalytische Umsetzung von Reaktionsmedien, insbesondere von gasförmigen Reaktionsmedien |
| DE60133473T2 (de) * | 2001-12-14 | 2009-05-20 | Evonik Stockhausen Gmbh | Verfahren zur Herstellung von Acrylsäure |
| US7294734B2 (en) * | 2003-05-02 | 2007-11-13 | Velocys, Inc. | Process for converting a hydrocarbon to an oxygenate or a nitrile |
| JP5006507B2 (ja) * | 2004-01-30 | 2012-08-22 | 株式会社日本触媒 | アクリル酸の製造方法 |
-
2006
- 2006-02-07 FR FR0601061A patent/FR2897059B1/fr not_active Expired - Fee Related
-
2007
- 2007-02-06 WO PCT/FR2007/050758 patent/WO2007090991A2/fr not_active Ceased
- 2007-02-06 AT AT07731584T patent/ATE430724T1/de not_active IP Right Cessation
- 2007-02-06 RU RU2008135966/04A patent/RU2397156C2/ru not_active IP Right Cessation
- 2007-02-06 CN CN2007800045903A patent/CN101400639B/zh not_active Expired - Fee Related
- 2007-02-06 JP JP2008551845A patent/JP5097128B2/ja not_active Expired - Fee Related
- 2007-02-06 US US12/278,016 patent/US7880034B2/en not_active Expired - Fee Related
- 2007-02-06 PL PL07731584T patent/PL1981835T3/pl unknown
- 2007-02-06 ES ES07731584T patent/ES2325695T3/es active Active
- 2007-02-06 DE DE602007001072T patent/DE602007001072D1/de active Active
- 2007-02-06 MY MYPI20083003A patent/MY139630A/en unknown
- 2007-02-06 EP EP07731584A patent/EP1981835B1/fr not_active Not-in-force
- 2007-02-06 PT PT07731584T patent/PT1981835E/pt unknown
- 2007-02-06 BR BRPI0707533-2A patent/BRPI0707533A2/pt not_active IP Right Cessation
- 2007-02-06 KR KR1020087019397A patent/KR101004593B1/ko not_active Expired - Fee Related
-
2008
- 2008-07-30 ZA ZA200806644A patent/ZA200806644B/xx unknown
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2606623C2 (ru) * | 2010-09-16 | 2017-01-10 | Басф Се | Способ получения акриловой кислоты из этанола и формальдегида |
| RU2610431C2 (ru) * | 2010-09-16 | 2017-02-10 | Басф Се | Способ получения акриловой кислоты из метанола и уксусной кислоты |
Also Published As
| Publication number | Publication date |
|---|---|
| BRPI0707533A2 (pt) | 2011-05-03 |
| US7880034B2 (en) | 2011-02-01 |
| CN101400639A (zh) | 2009-04-01 |
| FR2897059B1 (fr) | 2008-04-18 |
| KR101004593B1 (ko) | 2010-12-28 |
| PT1981835E (pt) | 2009-07-06 |
| US20090018362A1 (en) | 2009-01-15 |
| EP1981835A2 (fr) | 2008-10-22 |
| KR20080092429A (ko) | 2008-10-15 |
| ATE430724T1 (de) | 2009-05-15 |
| PL1981835T3 (pl) | 2009-11-30 |
| ES2325695T3 (es) | 2009-09-14 |
| WO2007090991A3 (fr) | 2007-12-06 |
| EP1981835B1 (fr) | 2009-05-06 |
| DE602007001072D1 (de) | 2009-06-18 |
| MY139630A (en) | 2009-10-30 |
| FR2897059A1 (fr) | 2007-08-10 |
| ZA200806644B (en) | 2009-05-27 |
| CN101400639B (zh) | 2012-05-30 |
| WO2007090991A2 (fr) | 2007-08-16 |
| RU2397156C2 (ru) | 2010-08-20 |
| JP2009524630A (ja) | 2009-07-02 |
| JP5097128B2 (ja) | 2012-12-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU2008135966A (ru) | Способ получения акриловой кислоты | |
| RU2008135988A (ru) | Способ получения акролеина | |
| JP2009524630A5 (ru) | ||
| RU2009135770A (ru) | Способы получения высших углеводородов из метана и брома | |
| MY157693A (en) | Method for preparing acrylic acid from glycerol | |
| DE60133473D1 (de) | Verfahren zur Herstellung von Acrylsäure | |
| EA201492001A1 (ru) | Способ получения химических соединений из диоксида углерода | |
| WO2006087083A3 (en) | Process for dehydrating glycerol to acrolein | |
| MY152299A (en) | Process for manufacturing acrolein from glycerol | |
| EA201400498A1 (ru) | Способ получения синтез-газа для производства метанола | |
| ATE307107T1 (de) | Verbessertes verfahren zur herstellung von carbonsäuren | |
| EA201400045A1 (ru) | Способ получения валеролактона из левулиновой кислоты | |
| RU2009131730A (ru) | Способ получения 1,2-пропандиола гидрогенолизом глицерина | |
| EA202192150A1 (ru) | Способ получения метилацетата карбонилированием диметилового эфира | |
| RU2012147025A (ru) | Способ получения оксалата газофазным способом с участием оксида углерода | |
| RU2012103891A (ru) | Способ производства фтороводорода | |
| CN108530318A (zh) | 一种合成己二腈的方法 | |
| EA202091358A1 (ru) | Способ получения гранулированного катализатора для процессов окисления | |
| RU2008108096A (ru) | Способ получения 4,4'-дифторбензофенона | |
| DE602006017608D1 (de) | Verfahren zur herstellung von schwefelsäure | |
| RU2004130288A (ru) | Способ получения соединения (мет)акриловой кислоты | |
| CN107915584A (zh) | 氟磺胺草醚中间体2‑氯‑4‑三氟甲基苯酚的合成方法 | |
| DK1902008T3 (da) | Højeffektiv fremgangsmåde til fremstilling af methanol ud af en syntesegas | |
| ATE538081T1 (de) | Oxidationsverfahren zur herstellung von essigsäure und ethylen | |
| CN103224489B (zh) | 一种提高埃索美拉唑生产收率和速率的方法 |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | The patent is invalid due to non-payment of fees |
Effective date: 20150207 |