MXPA04007238A - Control de procedimiento en la produccion de acido acetico utilizando la medicion de la densidad de la fase pesada. - Google Patents
Control de procedimiento en la produccion de acido acetico utilizando la medicion de la densidad de la fase pesada.Info
- Publication number
- MXPA04007238A MXPA04007238A MXPA04007238A MXPA04007238A MXPA04007238A MX PA04007238 A MXPA04007238 A MX PA04007238A MX PA04007238 A MXPA04007238 A MX PA04007238A MX PA04007238 A MXPA04007238 A MX PA04007238A MX PA04007238 A MXPA04007238 A MX PA04007238A
- Authority
- MX
- Mexico
- Prior art keywords
- reaction
- reaction mixture
- reactor
- methyl acetate
- heavy phase
- Prior art date
Links
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 title claims abstract description 132
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 24
- 238000004886 process control Methods 0.000 title claims abstract description 6
- 238000001739 density measurement Methods 0.000 title abstract description 7
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims abstract description 102
- 238000006243 chemical reaction Methods 0.000 claims abstract description 66
- 238000000034 method Methods 0.000 claims abstract description 57
- 230000006315 carbonylation Effects 0.000 claims abstract description 24
- 238000005810 carbonylation reaction Methods 0.000 claims abstract description 24
- 238000004821 distillation Methods 0.000 claims abstract description 11
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 claims description 66
- KXKVLQRXCPHEJC-UHFFFAOYSA-N acetic acid trimethyl ester Natural products COC(C)=O KXKVLQRXCPHEJC-UHFFFAOYSA-N 0.000 claims description 66
- 239000011541 reaction mixture Substances 0.000 claims description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- 239000003054 catalyst Substances 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 17
- INQOMBQAUSQDDS-UHFFFAOYSA-N iodomethane Chemical compound IC INQOMBQAUSQDDS-UHFFFAOYSA-N 0.000 claims description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 13
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 13
- 230000004044 response Effects 0.000 claims description 11
- 239000000047 product Substances 0.000 claims description 5
- 239000012429 reaction media Substances 0.000 claims description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 claims description 2
- 239000007795 chemical reaction product Substances 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims 1
- 230000008569 process Effects 0.000 abstract description 24
- 238000012544 monitoring process Methods 0.000 abstract description 14
- 238000000746 purification Methods 0.000 abstract description 6
- 239000012071 phase Substances 0.000 description 45
- 239000000523 sample Substances 0.000 description 8
- 230000007423 decrease Effects 0.000 description 7
- 230000008859 change Effects 0.000 description 6
- 230000001276 controlling effect Effects 0.000 description 5
- 230000003247 decreasing effect Effects 0.000 description 5
- 229910052703 rhodium Inorganic materials 0.000 description 5
- 239000010948 rhodium Substances 0.000 description 5
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 4
- 238000010924 continuous production Methods 0.000 description 4
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 239000000203 mixture Substances 0.000 description 4
- 230000002829 reductive effect Effects 0.000 description 4
- 238000005070 sampling Methods 0.000 description 4
- 238000004458 analytical method Methods 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000012512 characterization method Methods 0.000 description 3
- 230000000875 corresponding effect Effects 0.000 description 3
- 229910052741 iridium Inorganic materials 0.000 description 3
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000006073 displacement reaction Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 229910052736 halogen Inorganic materials 0.000 description 2
- 150000002367 halogens Chemical class 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- XMBWDFGMSWQBCA-UHFFFAOYSA-N hydrogen iodide Chemical compound I XMBWDFGMSWQBCA-UHFFFAOYSA-N 0.000 description 2
- HSZCZNFXUDYRKD-UHFFFAOYSA-M lithium iodide Chemical compound [Li+].[I-] HSZCZNFXUDYRKD-UHFFFAOYSA-M 0.000 description 2
- 229910052751 metal Inorganic materials 0.000 description 2
- 239000002184 metal Substances 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 235000019260 propionic acid Nutrition 0.000 description 2
- 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 2
- 230000009467 reduction Effects 0.000 description 2
- 238000005303 weighing Methods 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 159000000021 acetate salts Chemical class 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 150000001351 alkyl iodides Chemical class 0.000 description 1
- 239000000538 analytical sample Substances 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 238000001311 chemical methods and process Methods 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 230000003111 delayed effect Effects 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 208000028659 discharge Diseases 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 230000008713 feedback mechanism Effects 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 238000003780 insertion Methods 0.000 description 1
- 230000037431 insertion Effects 0.000 description 1
- XMBWDFGMSWQBCA-UHFFFAOYSA-M iodide Chemical compound [I-] XMBWDFGMSWQBCA-UHFFFAOYSA-M 0.000 description 1
- GKOZUEZYRPOHIO-UHFFFAOYSA-N iridium atom Chemical compound [Ir] GKOZUEZYRPOHIO-UHFFFAOYSA-N 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000011005 laboratory method Methods 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- XIXADJRWDQXREU-UHFFFAOYSA-M lithium acetate Chemical compound [Li+].CC([O-])=O XIXADJRWDQXREU-UHFFFAOYSA-M 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- -1 methyl iodide Chemical class 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 230000036961 partial effect Effects 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 150000004714 phosphonium salts Chemical group 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/10—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide
- C07C51/12—Preparation of carboxylic acids or their salts, halides or anhydrides by reaction with carbon monoxide on an oxygen-containing group in organic compounds, e.g. alcohols
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US10/058,547 US6677480B2 (en) | 2002-01-28 | 2002-01-28 | Process control in production of acetic acid via use of heavy phase density measurement |
| PCT/US2003/000503 WO2003064364A1 (en) | 2002-01-28 | 2003-01-09 | Process control in production of acetic acid via use of heavy phase density measurement |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| MXPA04007238A true MXPA04007238A (es) | 2004-10-29 |
Family
ID=27609612
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| MXPA04007238A MXPA04007238A (es) | 2002-01-28 | 2003-01-09 | Control de procedimiento en la produccion de acido acetico utilizando la medicion de la densidad de la fase pesada. |
Country Status (14)
| Country | Link |
|---|---|
| US (1) | US6677480B2 (enExample) |
| EP (1) | EP1470098B1 (enExample) |
| JP (1) | JP4263103B2 (enExample) |
| KR (1) | KR100922945B1 (enExample) |
| CN (1) | CN1279011C (enExample) |
| AT (1) | ATE431814T1 (enExample) |
| BR (1) | BR0306690A (enExample) |
| CA (1) | CA2466904C (enExample) |
| DE (1) | DE60327690D1 (enExample) |
| ES (1) | ES2327401T3 (enExample) |
| MX (1) | MXPA04007238A (enExample) |
| MY (1) | MY125742A (enExample) |
| TW (1) | TWI247003B (enExample) |
| WO (1) | WO2003064364A1 (enExample) |
Families Citing this family (28)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FI20040260A0 (fi) * | 2004-02-18 | 2004-02-18 | Forchem Oy | Menetelmä mäntyöljyn jalostamiseksi |
| US7271293B2 (en) * | 2004-03-02 | 2007-09-18 | Celanese International Corporation | Control method for process of removing permanganate reducing compounds from methanol carbonylation process |
| US7053241B1 (en) | 2005-02-24 | 2006-05-30 | Celanese International Corporation | Acetic acid production methods incorporating at least one metal salt as a catalyst stabilizer |
| DE102007037848B4 (de) | 2007-08-10 | 2009-09-10 | Siemens Ag | Kathode |
| US7619113B2 (en) * | 2007-09-27 | 2009-11-17 | Celanese International Corporation | Method and apparatus for making acetic acid with improved purification |
| US7790919B2 (en) * | 2008-03-17 | 2010-09-07 | Lyondell Chemical Technology, L.P. | Removing hydrocarbon impurities from acetic acid production process |
| US7790920B2 (en) * | 2008-09-11 | 2010-09-07 | Lyondell Chemical Technology, L.P. | Preparation of acetic acid |
| US8431740B2 (en) * | 2010-07-21 | 2013-04-30 | Equistar Chemicals, Lp | Controlling decanter phase separation of acetic acid production process |
| US8461379B2 (en) * | 2010-10-12 | 2013-06-11 | Celanese International Corporation | Production of acetic acid comprising feeding at least one reactant to a recycle stream |
| US8519182B2 (en) * | 2010-10-18 | 2013-08-27 | Lyondell Chemical Technology, L.P. | Acetic acid production process |
| US8916727B2 (en) | 2011-12-16 | 2014-12-23 | Celanese International Corporation | Production of acetic acid with enhanced catalyst stability |
| US9598342B2 (en) | 2013-03-15 | 2017-03-21 | Celanese International Corporation | Production of acetic acid with enhanced catalyst stability |
| CN104513143A (zh) * | 2013-09-26 | 2015-04-15 | 陶氏技术投资有限责任公司 | 加氢甲酰化方法 |
| US9302975B1 (en) | 2015-07-01 | 2016-04-05 | Celanese International Corporation | Process for flashing a reaction medium |
| US9233907B1 (en) | 2014-11-14 | 2016-01-12 | Celanese International Corporation | Reducing hydrogen iodide content in carbonylation processes |
| US9512056B2 (en) * | 2015-02-04 | 2016-12-06 | Celanese International Corporation | Process to control HI concentration in residuum stream |
| US9505696B2 (en) * | 2015-02-04 | 2016-11-29 | Celanese International Corporation | Process to control HI concentration in residuum stream |
| US9302974B1 (en) | 2015-07-01 | 2016-04-05 | Celanese International Corporation | Process for producing acetic acid |
| US9382183B1 (en) | 2015-07-01 | 2016-07-05 | Celanese International Corporation | Process for flashing a reaction medium |
| CN108137468B (zh) | 2015-10-02 | 2021-04-13 | 国际人造丝公司 | 使用水的再循环生产乙酸的方法 |
| US9957216B2 (en) | 2015-11-13 | 2018-05-01 | Celanese International Corporation | Processes for producing acetic acid |
| US9908835B2 (en) | 2015-11-13 | 2018-03-06 | Celanese International Corporation | Processes for purifying acetic and hydrating anhydride |
| US10807935B2 (en) | 2018-11-02 | 2020-10-20 | Celanese International Corporation | Process for continuous acetic acid production |
| US20230127564A1 (en) | 2020-04-01 | 2023-04-27 | Celanese International Corporation | Processes for removing and/or reducing permanganate reducing compounds and alkyl iodides |
| JP2023528451A (ja) | 2020-06-03 | 2023-07-04 | セラニーズ・インターナショナル・コーポレーション | 酢酸の製造及び精製 |
| KR20230019135A (ko) | 2020-06-03 | 2023-02-07 | 셀라니즈 인터내셔날 코포레이션 | 공정 스트림으로부터 아세탈의 제거 |
| MX2022015384A (es) | 2020-06-03 | 2023-01-16 | Celanese Int Corp | Proceso para la produccion de acido acetico mediante la eliminacion de compuestos reductores de permanganato. |
| CN113295819B (zh) * | 2021-06-30 | 2024-08-13 | 内蒙古易高煤化科技有限公司 | 一种气相甲醇羰基氧化法制碳酸二甲酯的催化剂评价装置 |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3769329A (en) | 1970-03-12 | 1973-10-30 | Monsanto Co | Production of carboxylic acids and esters |
| US5144068A (en) | 1984-05-03 | 1992-09-01 | Hoechst Celanese Corporation | Methanol carbonylation process |
| US5026908A (en) | 1984-05-03 | 1991-06-25 | Hoechst Celanese Corporation | Methanol carbonylation process |
| US5001259A (en) | 1984-05-03 | 1991-03-19 | Hoechst Celanese Corporation | Methanol carbonylation process |
| US5352415A (en) * | 1993-09-29 | 1994-10-04 | Hoechst Celanese Corporation | Control system for acetic acid manufacturing process |
| US5374774A (en) * | 1994-03-11 | 1994-12-20 | Hoechst Celanese Corporation | Control system for an acetic acid manufacturing process |
| US5474774A (en) | 1994-03-25 | 1995-12-12 | Jlb, Inc. | Adhesion inhibiting composition |
| US5554790A (en) * | 1994-04-04 | 1996-09-10 | Daicel Chemical Industries, Ltd. | Process for producing acetic anhydride and acetic acid |
| JP3308392B2 (ja) * | 1994-06-02 | 2002-07-29 | ダイセル化学工業株式会社 | カルボニル化反応方法 |
| EP0768295B1 (en) * | 1995-04-27 | 2000-08-16 | Daicel Chemical Industries, Ltd. | Process for producing acetic acid |
| GB9816564D0 (en) * | 1998-07-31 | 1998-09-30 | Bp Chem Int Ltd | Process |
| GB9819079D0 (en) * | 1998-09-03 | 1998-10-28 | Bp Chem Int Ltd | Carbonylation process |
| GB9825424D0 (en) | 1998-11-19 | 1999-01-13 | Bp Chem Int Ltd | Process |
| US6552221B1 (en) * | 1998-12-18 | 2003-04-22 | Millenium Petrochemicals, Inc. | Process control for acetic acid manufacture |
| US6103934A (en) * | 1998-12-18 | 2000-08-15 | Millennium Petrochemicals, Inc. | Manufacturing and process control methods |
-
2002
- 2002-01-28 US US10/058,547 patent/US6677480B2/en not_active Expired - Lifetime
-
2003
- 2003-01-09 KR KR1020047011568A patent/KR100922945B1/ko not_active Expired - Fee Related
- 2003-01-09 AT AT03701257T patent/ATE431814T1/de not_active IP Right Cessation
- 2003-01-09 BR BR0306690-8A patent/BR0306690A/pt not_active IP Right Cessation
- 2003-01-09 ES ES03701257T patent/ES2327401T3/es not_active Expired - Lifetime
- 2003-01-09 DE DE60327690T patent/DE60327690D1/de not_active Expired - Lifetime
- 2003-01-09 MX MXPA04007238A patent/MXPA04007238A/es active IP Right Grant
- 2003-01-09 CA CA2466904A patent/CA2466904C/en not_active Expired - Fee Related
- 2003-01-09 CN CNB038028026A patent/CN1279011C/zh not_active Expired - Fee Related
- 2003-01-09 JP JP2003563990A patent/JP4263103B2/ja not_active Expired - Fee Related
- 2003-01-09 EP EP03701257A patent/EP1470098B1/en not_active Revoked
- 2003-01-09 WO PCT/US2003/000503 patent/WO2003064364A1/en not_active Ceased
- 2003-01-27 MY MYPI20030262A patent/MY125742A/en unknown
- 2003-01-28 TW TW092101827A patent/TWI247003B/zh not_active IP Right Cessation
Also Published As
| Publication number | Publication date |
|---|---|
| ATE431814T1 (de) | 2009-06-15 |
| CN1279011C (zh) | 2006-10-11 |
| MY125742A (en) | 2006-08-30 |
| TWI247003B (en) | 2006-01-11 |
| EP1470098B1 (en) | 2009-05-20 |
| CA2466904A1 (en) | 2003-08-07 |
| EP1470098A1 (en) | 2004-10-27 |
| JP2005516058A (ja) | 2005-06-02 |
| JP4263103B2 (ja) | 2009-05-13 |
| ES2327401T3 (es) | 2009-10-29 |
| DE60327690D1 (de) | 2009-07-02 |
| TW200305563A (en) | 2003-11-01 |
| US6677480B2 (en) | 2004-01-13 |
| KR100922945B1 (ko) | 2009-10-22 |
| KR20040086299A (ko) | 2004-10-08 |
| CN1622928A (zh) | 2005-06-01 |
| CA2466904C (en) | 2010-07-20 |
| BR0306690A (pt) | 2004-12-07 |
| WO2003064364A1 (en) | 2003-08-07 |
| US20030144548A1 (en) | 2003-07-31 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FG | Grant or registration |