CN102137833A - 泡沫体在用于制备不饱和醛或羧酸的氧化反应器中的用途 - Google Patents
泡沫体在用于制备不饱和醛或羧酸的氧化反应器中的用途 Download PDFInfo
- Publication number
- CN102137833A CN102137833A CN2009801334219A CN200980133421A CN102137833A CN 102137833 A CN102137833 A CN 102137833A CN 2009801334219 A CN2009801334219 A CN 2009801334219A CN 200980133421 A CN200980133421 A CN 200980133421A CN 102137833 A CN102137833 A CN 102137833A
- Authority
- CN
- China
- Prior art keywords
- reactor
- oxidation
- foams
- carboxylic acid
- dehydrogenation
- 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.)
- Granted
Links
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 275
- 230000003647 oxidation Effects 0.000 title claims abstract description 274
- 239000006260 foam Substances 0.000 title claims abstract description 160
- 150000001735 carboxylic acids Chemical class 0.000 title claims abstract 32
- 150000001299 aldehydes Chemical class 0.000 title claims description 34
- 239000000463 material Substances 0.000 claims abstract description 202
- 238000000034 method Methods 0.000 claims abstract description 127
- 239000003054 catalyst Substances 0.000 claims abstract description 117
- 238000006356 dehydrogenation reaction Methods 0.000 claims abstract description 107
- 229930195735 unsaturated hydrocarbon Natural products 0.000 claims abstract description 42
- 230000003197 catalytic effect Effects 0.000 claims abstract description 30
- 239000007789 gas Substances 0.000 claims abstract description 22
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 11
- 239000001301 oxygen Substances 0.000 claims abstract description 11
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 11
- 238000006243 chemical reaction Methods 0.000 claims description 59
- HGINCPLSRVDWNT-UHFFFAOYSA-N Acrolein Chemical compound C=CC=O HGINCPLSRVDWNT-UHFFFAOYSA-N 0.000 claims description 49
- 239000003795 chemical substances by application Substances 0.000 claims description 42
- 238000006555 catalytic reaction Methods 0.000 claims description 41
- 238000012545 processing Methods 0.000 claims description 39
- 239000004215 Carbon black (E152) Substances 0.000 claims description 36
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 claims description 36
- 229930195733 hydrocarbon Natural products 0.000 claims description 36
- 150000002430 hydrocarbons Chemical class 0.000 claims description 36
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 33
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 33
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 30
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical group CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 claims description 28
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 claims description 28
- NIXOWILDQLNWCW-UHFFFAOYSA-N Acrylic acid Chemical compound OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 23
- 239000008246 gaseous mixture Substances 0.000 claims description 23
- 239000000725 suspension Substances 0.000 claims description 23
- STNJBCKSHOAVAJ-UHFFFAOYSA-N Methacrolein Chemical compound CC(=C)C=O STNJBCKSHOAVAJ-UHFFFAOYSA-N 0.000 claims description 21
- 239000012071 phase Substances 0.000 claims description 15
- 238000002360 preparation method Methods 0.000 claims description 15
- 239000001294 propane Substances 0.000 claims description 15
- 238000002425 crystallisation Methods 0.000 claims description 12
- 230000008025 crystallization Effects 0.000 claims description 11
- 239000000376 reactant Substances 0.000 claims description 11
- 239000012530 fluid Substances 0.000 claims description 10
- 238000012856 packing Methods 0.000 claims description 10
- 239000000126 substance Substances 0.000 claims description 10
- 239000012808 vapor phase Substances 0.000 claims description 10
- 230000008569 process Effects 0.000 claims description 9
- 238000000605 extraction Methods 0.000 claims description 8
- 239000002904 solvent Substances 0.000 claims description 8
- 239000000654 additive Substances 0.000 claims description 5
- 230000000996 additive effect Effects 0.000 claims description 5
- 238000004821 distillation Methods 0.000 claims description 4
- 238000010526 radical polymerization reaction Methods 0.000 claims description 4
- 239000011877 solvent mixture Substances 0.000 claims description 4
- 150000001732 carboxylic acid derivatives Chemical class 0.000 abstract description 53
- 239000000203 mixture Substances 0.000 abstract description 22
- 229920000642 polymer Polymers 0.000 abstract description 9
- 229930195734 saturated hydrocarbon Natural products 0.000 abstract description 8
- 230000001590 oxidative effect Effects 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 abstract 3
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 31
- 229910045601 alloy Inorganic materials 0.000 description 24
- 239000000956 alloy Substances 0.000 description 24
- 230000008859 change Effects 0.000 description 14
- 239000000047 product Substances 0.000 description 14
- 239000000919 ceramic Substances 0.000 description 13
- 230000000694 effects Effects 0.000 description 12
- 239000000243 solution Substances 0.000 description 12
- 238000000576 coating method Methods 0.000 description 11
- 239000011248 coating agent Substances 0.000 description 10
- 229910052751 metal Inorganic materials 0.000 description 10
- 239000002184 metal Substances 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 6
- 150000002894 organic compounds Chemical class 0.000 description 5
- 238000010791 quenching Methods 0.000 description 5
- 230000000171 quenching effect Effects 0.000 description 5
- 229920006395 saturated elastomer Polymers 0.000 description 5
- 239000000470 constituent Substances 0.000 description 4
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 3
- 229910010413 TiO 2 Inorganic materials 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 239000002638 heterogeneous catalyst Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000007769 metal material Substances 0.000 description 3
- 239000011541 reaction mixture Substances 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- SOGAXMICEFXMKE-UHFFFAOYSA-N Butylmethacrylate Chemical compound CCCCOC(=O)C(C)=C SOGAXMICEFXMKE-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- OVBPIULPVIDEAO-LBPRGKRZSA-N folic acid Chemical compound C=1N=C2NC(N)=NC(=O)C2=NC=1CNC1=CC=C(C(=O)N[C@@H](CCC(O)=O)C(O)=O)C=C1 OVBPIULPVIDEAO-LBPRGKRZSA-N 0.000 description 2
- 238000010528 free radical solution polymerization reaction Methods 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 238000005457 optimization Methods 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- HBMJWWWQQXIZIP-UHFFFAOYSA-N silicon carbide Chemical compound [Si+]#[C-] HBMJWWWQQXIZIP-UHFFFAOYSA-N 0.000 description 2
- 229910010271 silicon carbide Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 230000001131 transforming effect Effects 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- JHPBZFOKBAGZBL-UHFFFAOYSA-N (3-hydroxy-2,2,4-trimethylpentyl) 2-methylprop-2-enoate Chemical compound CC(C)C(O)C(C)(C)COC(=O)C(C)=C JHPBZFOKBAGZBL-UHFFFAOYSA-N 0.000 description 1
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 description 1
- LDHQCZJRKDOVOX-UHFFFAOYSA-N 2-butenoic acid Chemical compound CC=CC(O)=O LDHQCZJRKDOVOX-UHFFFAOYSA-N 0.000 description 1
- 229920002972 Acrylic fiber Polymers 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical class [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- SXRSQZLOMIGNAQ-UHFFFAOYSA-N Glutaraldehyde Chemical compound O=CCCCC=O SXRSQZLOMIGNAQ-UHFFFAOYSA-N 0.000 description 1
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 1
- FFEARJCKVFRZRR-BYPYZUCNSA-N L-methionine Chemical compound CSCC[C@H](N)C(O)=O FFEARJCKVFRZRR-BYPYZUCNSA-N 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- OVBPIULPVIDEAO-UHFFFAOYSA-N N-Pteroyl-L-glutaminsaeure Natural products C=1N=C2NC(N)=NC(=O)C2=NC=1CNC1=CC=C(C(=O)NC(CCC(O)=O)C(O)=O)C=C1 OVBPIULPVIDEAO-UHFFFAOYSA-N 0.000 description 1
- 239000006057 Non-nutritive feed additive Substances 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000011149 active material Substances 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 125000005907 alkyl ester group Chemical group 0.000 description 1
- 150000004645 aluminates Chemical class 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052787 antimony Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 229910052785 arsenic Inorganic materials 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 229910052728 basic metal Inorganic materials 0.000 description 1
- 150000003818 basic metals Chemical class 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000004568 cement Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000001186 cumulative effect Effects 0.000 description 1
- 239000013530 defoamer Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 229960000304 folic acid Drugs 0.000 description 1
- 235000019152 folic acid Nutrition 0.000 description 1
- 239000011724 folic acid Substances 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 229910052745 lead Inorganic materials 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000006262 metallic foam Substances 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 125000005395 methacrylic acid group Chemical group 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- 229930182817 methionine Natural products 0.000 description 1
- 229910003455 mixed metal oxide Inorganic materials 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000005839 oxidative dehydrogenation reaction Methods 0.000 description 1
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000010422 painting Methods 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- MHWRYTCHHJGQFQ-UHFFFAOYSA-N prop-2-enoic acid hydrate Chemical compound O.OC(=O)C=C MHWRYTCHHJGQFQ-UHFFFAOYSA-N 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 229960001866 silicon dioxide Drugs 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 229920000247 superabsorbent polymer Polymers 0.000 description 1
- 238000010557 suspension polymerization reaction Methods 0.000 description 1
- 229910052718 tin Inorganic materials 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
- 239000003643 water by type Substances 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Images
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
- 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
- B01J8/06—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 in tube reactors; the solid particles being arranged in tubes
- B01J8/067—Heating or cooling 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
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/248—Reactors comprising multiple separated flow channels
- B01J19/249—Plate-type 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
- B01J23/8885—Tungsten containing also molybdenum
-
- B01J35/56—
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0219—Coating the coating containing organic compounds
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0215—Coating
- B01J37/0225—Coating of metal substrates
-
- 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
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/32—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with formation of free hydrogen
- C07C5/327—Formation of non-aromatic carbon-to-carbon double bonds only
- C07C5/333—Catalytic processes
-
- 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
- C07C51/25—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring
- C07C51/252—Preparation of carboxylic acids or their salts, halides or anhydrides by oxidation with molecular oxygen of unsaturated compounds containing no six-membered aromatic ring of propene, butenes, acrolein or methacrolein
-
- 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
- B01J2208/00212—Plates; Jackets; Cylinders
- B01J2208/00221—Plates; Jackets; Cylinders comprising baffles for guiding the flow of the heat exchange medium
-
- 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
- B01J2208/02—Processes carried out in the presence of solid particles; Reactors therefor with stationary particles
- B01J2208/023—Details
- B01J2208/024—Particulate material
- B01J2208/025—Two or more types of catalyst
-
- 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
- B01J2219/00002—Chemical plants
- B01J2219/00004—Scale aspects
- B01J2219/00006—Large-scale industrial plants
-
- 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
- B01J2219/00002—Chemical plants
- B01J2219/00027—Process aspects
- B01J2219/0004—Processes 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
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2451—Geometry of the reactor
- B01J2219/2453—Plates arranged in parallel
-
- 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
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2476—Construction materials
- B01J2219/2477—Construction materials of the catalysts
- B01J2219/2479—Catalysts coated on the surface of plates or inserts
-
- 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
- B01J2219/24—Stationary reactors without moving elements inside
- B01J2219/2401—Reactors comprising multiple separate flow channels
- B01J2219/245—Plate-type reactors
- B01J2219/2476—Construction materials
- B01J2219/2477—Construction materials of the catalysts
- B01J2219/2481—Catalysts in granular from between plates
-
- 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
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
-
- 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
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
Description
Claims (35)
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102008044946.6A DE102008044946B4 (de) | 2008-08-29 | 2008-08-29 | Einsatz von Schaumkörpern in Oxidations-Reaktoren zur Herstellung ungesättigter Carbonsäuren |
DE102008044946.6 | 2008-08-29 | ||
PCT/EP2009/059782 WO2010023053A2 (de) | 2008-08-29 | 2009-07-29 | Einsatz von schaumkörpern in oxidations-reaktoren zur herstellung ungesättigter aldehyde oder carbonsäuren |
Publications (2)
Publication Number | Publication Date |
---|---|
CN102137833A true CN102137833A (zh) | 2011-07-27 |
CN102137833B CN102137833B (zh) | 2014-04-16 |
Family
ID=41571540
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN200980133421.9A Active CN102137833B (zh) | 2008-08-29 | 2009-07-29 | 泡沫体在用于制备不饱和醛或羧酸的氧化反应器中的用途 |
Country Status (8)
Country | Link |
---|---|
US (1) | US8841481B2 (zh) |
EP (1) | EP2315738B1 (zh) |
JP (1) | JP2012500820A (zh) |
CN (1) | CN102137833B (zh) |
BR (1) | BRPI0914143A8 (zh) |
DE (1) | DE102008044946B4 (zh) |
WO (1) | WO2010023053A2 (zh) |
ZA (1) | ZA201102225B (zh) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109789389A (zh) * | 2016-09-30 | 2019-05-21 | 赢创德固赛有限公司 | 包含金属泡沫体的固定催化床 |
CN114225848A (zh) * | 2022-02-24 | 2022-03-25 | 北京弗莱明科技有限公司 | 一种高收率连续氧化制备丁烯-2-酸的装置和方法 |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102005039156B4 (de) | 2005-08-17 | 2014-12-24 | Evonik Degussa Gmbh | Verfahren zur Herstellung von (Meth)Acrylsäure mit Schwersiedeaufarbeitung durch Kristallisation |
DE102006039203B4 (de) | 2006-08-22 | 2014-06-18 | Evonik Degussa Gmbh | Verfahren zur Herstellung von durch Kristallisation gereinigter Acrylsäure aus Hydroxypropionsäure sowie Vorrichtung dazu |
JP6069224B2 (ja) | 2011-01-31 | 2017-02-01 | アプライズ バイオ, インコーポレイテッド | 細胞において複数のエピトープを同定する方法 |
DE102012005659B4 (de) * | 2012-03-22 | 2015-10-01 | Otto-Von-Guericke-Universität Magdeburg | Füllkörper für den Einsatz in Wärmeübertragern und Wärmeübertrager mit Füllkörpern |
WO2014026032A2 (en) | 2012-08-08 | 2014-02-13 | Apprise Bio, Inc. | Increasing dynamic range for identifying multiple epitopes in cells |
DE102013000602A1 (de) | 2013-01-16 | 2014-07-17 | Evonik Industries Ag | Verfahren zur Herstellung von Acrylsäure |
DE102013217386A1 (de) | 2013-09-02 | 2015-03-05 | Evonik Industries Ag | Verfahren zur Herstellung von Acrylsäure |
ITMI20131439A1 (it) * | 2013-09-03 | 2015-03-04 | Eni Spa | Reattore tubolare a letto impaccato per reazioni catalitiche eterogenee esotermiche o endotermiche |
TWI592209B (zh) * | 2016-03-31 | 2017-07-21 | 國立清華大學 | 反應器及其溫度的控制方法 |
PL3246303T3 (pl) | 2016-05-19 | 2020-06-01 | Evonik Operations Gmbh | Wytwarzanie n-pentanalu z mieszanin surowców ubogich w buten |
US11493274B2 (en) * | 2019-12-04 | 2022-11-08 | Greyrock Technology, Llc | Process for the commercial production of high-quality catalyst materials |
EP3597295A1 (en) * | 2018-07-20 | 2020-01-22 | Alantum Europe GmbH | Catalyst material and method of manufacturing the same |
EP3892367A1 (en) * | 2020-04-09 | 2021-10-13 | Röhm GmbH | A tube bundle reactor and method for the production of methacrylic acid through the partial oxidation of methacrolein |
DE102021203883B4 (de) * | 2021-04-19 | 2023-02-09 | Hydrogenious Lohc Technologies Gmbh | Verfahren zum Bereitstellen von Wasserstoffgas |
Family Cites Families (92)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3087807A (en) | 1959-12-04 | 1963-04-30 | United Aircraft Corp | Method of making foamed metal |
US3161670A (en) | 1960-12-12 | 1964-12-15 | Shell Oil Co | Preparation of olefinic compounds |
US3090094A (en) | 1961-02-21 | 1963-05-21 | Gen Motors Corp | Method of making porous ceramic articles |
NL6918448A (zh) | 1968-12-16 | 1970-06-18 | ||
US3670044A (en) | 1969-07-18 | 1972-06-13 | Phillips Petroleum Co | Catalytic dehydrogenation process |
US4220091A (en) | 1978-03-03 | 1980-09-02 | The United States Of America As Represented By The Secretary Of The Army | Delay fuze for explosive charge |
USRE32082E (en) | 1982-04-14 | 1986-02-11 | The Halcon Sd Group, Inc. | Conversion of isobutane to methacrolein |
US4532365A (en) | 1982-09-20 | 1985-07-30 | The Halcon Sd Group, Inc. | Conversion of alkanes to unsaturated aldehydes |
US4535188A (en) | 1982-04-14 | 1985-08-13 | The Halcon Sd Group, Inc. | Conversion of isobutane to methacrolein |
US4413147A (en) | 1982-04-14 | 1983-11-01 | The Halcon Sd Group, Inc. | Conversion of isobutane to methacrolein |
CA1217502A (en) | 1982-04-14 | 1987-02-03 | Sargis Khoobiar | Conversion of alkanes to unsaturated aldehydes |
EP0117146B1 (en) | 1983-02-22 | 1986-12-30 | The Halcon Sd Group, Inc. | Conversion of propane to acrylic acid |
US4788371A (en) | 1987-12-30 | 1988-11-29 | Uop Inc. | Catalytic oxidative steam dehydrogenation process |
JPH0784400B2 (ja) | 1990-04-03 | 1995-09-13 | 株式会社日本触媒 | 不飽和アルデヒドおよび不飽和酸の製造方法 |
DE4101630A1 (de) | 1990-06-08 | 1991-12-12 | Fraunhofer Ges Forschung | Verfahren zur herstellung aufschaeumbarer metallkoerper und verwendung derselben |
DE4018360C1 (en) | 1990-06-08 | 1991-05-29 | Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung Ev, 8000 Muenchen, De | Porous metal body prodn. - involves compaction at low temp. followed by heating to near melting point of metal |
US5344805A (en) | 1993-05-03 | 1994-09-06 | Phillips Petroleum Company | Platinum and tin-containing catalyst and use thereof in alkane dehydrogenation |
NO179131C (no) | 1993-06-14 | 1996-08-14 | Statoil As | Katalysator, fremgangsmåte for dens fremstilling og fremgangsmåte for dehydrogenering av lette paraffiner |
DE59603316D1 (de) | 1995-03-10 | 1999-11-18 | Basf Ag | Verfahren zur Herstellung von Acrolein, Acrylsäure oder deren Gemisch aus Propan |
DE19740252A1 (de) | 1997-09-12 | 1999-03-18 | Basf Ag | Verfahren zur Herstellung von Acrylsäure und Methacrylsäure |
US5877369A (en) | 1997-10-23 | 1999-03-02 | Phillips Petroleum Company | Hydrocarbon conversion catalyst composition and processes therefor and therewith |
DE19756292C2 (de) | 1997-12-10 | 1999-10-28 | Mannesmann Ag | Katalysator zur Umwandlung paraffinischer Kohlenwasserstoffe in korrespondierende Olefine |
NO307693B1 (no) | 1998-03-13 | 2000-05-15 | Statoil Asa | Forbedret katalysatorbaerermateriale, fremgangsmate for fremstilling derav, dehydrogeneringskatalysator, og katalytisk dehydrogenering av lette alkaner |
US6540975B2 (en) | 1998-07-27 | 2003-04-01 | Battelle Memorial Institute | Method and apparatus for obtaining enhanced production rate of thermal chemical reactions |
US6616909B1 (en) | 1998-07-27 | 2003-09-09 | Battelle Memorial Institute | Method and apparatus for obtaining enhanced production rate of thermal chemical reactions |
CN1229313C (zh) | 1998-09-03 | 2005-11-30 | 陶氏环球技术公司 | 用于制备烯烃的自热方法 |
DE19840277A1 (de) | 1998-09-04 | 2000-03-09 | Degussa | Verfahren zur Reduzierung des Gehalts an Acetalen oder Ketalen in alkoholischen Reaktionsgemischen |
DE19844325A1 (de) | 1998-09-28 | 2000-03-30 | Degussa | Verfahren zur Herstellung von Alkoholen durch katalytische Hydrierung von Aldehyden oder Ketonen |
DE19937105A1 (de) | 1999-08-06 | 2001-02-08 | Basf Ag | Oxidkatalysatoren |
DE19937196A1 (de) | 1999-08-06 | 2001-03-01 | Voith Paper Patent Gmbh | Einführhilfsvorrichtung zum Einführen des Anfangs einer Materialbahn in eine Walzenmaschine |
DE19937107A1 (de) | 1999-08-06 | 2001-02-08 | Basf Ag | Katalysator mit bimodaler Porenradienverteilung |
DE19953185A1 (de) | 1999-11-05 | 2001-05-23 | Degussa | Verfahren zur Herstellung von Wasserstoffperoxid |
US20020038051A1 (en) | 2000-02-18 | 2002-03-28 | Degussa-Huls Ag | Raney copper |
DE10028582A1 (de) | 2000-06-14 | 2001-12-20 | Basf Ag | Verfahren zur Herstellung von Acrolein oder Acrylsäure oder deren Gemischen aus Propan |
DE10051419A1 (de) | 2000-10-17 | 2002-04-18 | Basf Ag | Katalysator bestehend aus einem Trägerkörper und einer auf der Oberfläche des Trägerkörpers aufgebrachten katalytisch aktiven Oxidmasse |
DE10118814A1 (de) | 2001-04-17 | 2002-10-24 | Basf Ag | Verfahren zur Herstellung von Acrylsäure durch heterogen katalysierte Gasphasenoxidation von Propen mit molekularem Sauerstoff in einer Reaktionszone |
EP1642879B1 (de) | 2000-06-14 | 2014-05-21 | Basf Se | Verfahren zur Herstellung von Acrolein oder Acrylsäure oder deren Gemisch aus Propan |
DE10122027A1 (de) | 2001-05-07 | 2002-05-23 | Basf Ag | Verfahren zur Herstellung von Acrylsäure durch heterogen katalysierte Partialoxidation von Propan |
BR0112557B1 (pt) | 2000-07-18 | 2012-01-24 | processo para a preparação de ácido acrìlico, e, uso de um material de óxido multimetálico. | |
DE10044656B4 (de) | 2000-09-04 | 2005-12-29 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Offenzellige Siliciumcarbid-Schaumkeramik und Verfahren zu ihrer Herstellung |
CA2434162C (en) | 2001-01-05 | 2010-02-02 | National Institute Of Advanced Industrial Science And Technology | Reaction method utilizing diaphram type catalyst and apparatus therefor |
JP2002205968A (ja) * | 2001-01-05 | 2002-07-23 | National Institute Of Advanced Industrial & Technology | 隔膜型触媒を備えた反応装置 |
DE50115570D1 (de) | 2001-01-08 | 2010-09-09 | Evonik Degussa Gmbh | Verfahren zur Epoxidierung von Olefinen |
WO2002055469A1 (de) | 2001-01-12 | 2002-07-18 | Degussa Ag | Kontinuierliches verfahren zur herstellung und aufreinigung von (meth) acrylsäure |
US6596881B2 (en) | 2001-06-13 | 2003-07-22 | Degussa Ag | Process for the epoxidation of olefins |
US6600055B2 (en) | 2001-06-13 | 2003-07-29 | Degussa Ag | Process for the epoxidation of olefins |
US7176335B2 (en) | 2001-06-29 | 2007-02-13 | Basf Aktiengesellschaft | Method for producing methacrolein from isobutane |
DE10131297A1 (de) | 2001-06-29 | 2003-01-09 | Basf Ag | Verfahren zur Herstellung von partiellen Oxidationsprodukten und/oder partiellen Ammoxidationsprodukten wenigstens eines olefinischen Kohlenwasserstoffs |
CN1219737C (zh) | 2001-06-29 | 2005-09-21 | 巴斯福股份公司 | 由异丁烷制备甲基丙烯酸的方法 |
DE10211275A1 (de) | 2002-03-13 | 2003-09-25 | Basf Ag | Verfahren der kontinuierlichen heterogen katalysierten partiellen Dehydrierung |
EP1404647A1 (de) | 2001-06-29 | 2004-04-07 | Basf Aktiengesellschaft | Verfahren zur herstellung von ungesättigten nitrilen aus alkanen |
DE10142620A1 (de) | 2001-08-31 | 2003-03-20 | Degussa | Ammoximation von Ketonen und Aufarbeitung durch Pervaporation/Dampfpermeation |
MXPA02011489A (es) * | 2001-12-04 | 2003-06-30 | Rohm & Haas | Procesos mejorados para la preparacion de olefinas, acidos carboxilicos insaturados y nitrilos insaturados, a partir de alcanos. |
EP1319648B1 (en) * | 2001-12-14 | 2008-04-02 | Stockhausen GmbH | Process for the production of acrylic acid |
DE10211686A1 (de) | 2002-03-15 | 2003-10-02 | Stockhausen Chem Fab Gmbh | (Meth)Acrylsäurekristall und Verfahren zur Herstellung und Aufreinigung von wässriger (Meth)Acrylsäure |
US7045657B2 (en) * | 2002-04-03 | 2006-05-16 | Nippon Shokubai Co., Ltd. | Catalytic gas phase oxidation process |
DE10245585A1 (de) | 2002-09-27 | 2004-04-08 | Basf Ag | Verfahren zur Herstellung von wenigstens einem partiellen Oxidations- und/oder Ammoxidationsprodukt des Propylens |
US7038080B2 (en) | 2002-09-27 | 2006-05-02 | Basf Aktiengesellschaft | Heterogeneously catalyzed gas-phase partial oxidation of acrolein to acrylic acid |
US7238827B2 (en) | 2002-09-27 | 2007-07-03 | Basf Aktiengesellschaft | Preparation of at least one partial oxidation and/or ammoxidation product of propylene |
US7038082B2 (en) | 2002-10-17 | 2006-05-02 | Basf Aktiengesellschaft | Preparation of a multimetal oxide material |
DE10315215A1 (de) * | 2003-04-03 | 2004-10-14 | Basf Ag | In-situ Neubeschichtung von Katalysatorschüttungen |
US7294734B2 (en) | 2003-05-02 | 2007-11-13 | Velocys, Inc. | Process for converting a hydrocarbon to an oxygenate or a nitrile |
DE10335958A1 (de) * | 2003-08-04 | 2005-02-24 | Basf Ag | Verfahren zur Herstellung wässriger Polymerisatdispersionen |
US20050176985A1 (en) | 2003-11-13 | 2005-08-11 | Bogan Leonard E.Jr. | Processes for the preparation of olefins, unsaturated carboxylic acids and unsaturated nitriles from alkanes |
JP2005144432A (ja) * | 2003-11-18 | 2005-06-09 | Rohm & Haas Co | アルカンをアルケン、およびそれらの対応する酸素化生成物に転化するための触媒系 |
EP1598110A1 (en) * | 2004-04-22 | 2005-11-23 | Rohm and Haas Company | Structured oxidation catalysts |
DE102004030943B4 (de) | 2004-06-26 | 2013-10-02 | Evonik Oxeno Gmbh | Verfahren zur Herstellung von tert.-Butanol aus Isobuten-haltigen Kohlenwasserstoffgemischen |
US20060001711A1 (en) | 2004-06-30 | 2006-01-05 | Lexmark International, Inc. | Inkjet printhead with multiple ink reservoirs |
DE102004032129A1 (de) | 2004-07-01 | 2005-03-03 | Basf Ag | Verfahren zur Herstellung von Acrolein, oder Acrylsäure oder deren Gemisch aus Propan |
DE102005009885A1 (de) | 2005-03-01 | 2006-09-14 | Basf Ag | Verfahren zur Herstellung von Acrolein oder Acrylsäure oder deren Gemisch durch heterogen katalysierte partielle Gasphasenoxidation von Propylen |
JP5021467B2 (ja) | 2004-07-01 | 2012-09-05 | ビーエーエスエフ ソシエタス・ヨーロピア | プロピレンの不均一触媒部分気相酸化によるアクロレイン、アクリル酸、またはその混合物の製造方法 |
JP5156375B2 (ja) | 2004-07-01 | 2013-03-06 | ビーエーエスエフ ソシエタス・ヨーロピア | プロパンからのアクロレインもしくはアクリル酸またはそれらの混合物の製造 |
DE102005013039A1 (de) | 2005-03-18 | 2006-09-21 | Basf Ag | Verfahren zur Herstellung von Acrolein, oder Acrylsäure oder deren Gemisch aus Propan |
US7592483B2 (en) | 2004-07-01 | 2009-09-22 | Basf Aktiengesellschaft | Preparation of acrolein or acrylic acid or a mixture thereof by heterogeneously catalyzed partial gas phase oxidation of propylene |
DE102005010111A1 (de) | 2005-03-02 | 2006-09-07 | Basf Ag | Verfahren zur Herstellung von Acrylsäure durch heterogen katalysierte partielle Gasphasenoxidation von Propylen |
DE102005009891A1 (de) | 2005-03-01 | 2006-09-07 | Basf Ag | Verfahren zur Herstellung von Acrylsäure durch heterogen katalysierte partielle Gasphasenoxidation von Propylen |
US7569196B2 (en) | 2004-09-16 | 2009-08-04 | Oxeno Olefinchemie Gmbh | Device for carrying out liquid reactions with fine-grained solid catalysts and method for the use thereof |
TWI529181B (zh) | 2005-02-28 | 2016-04-11 | 贏創德固賽有限責任公司 | 以可更新原料為基之吸水聚合物結構及其生產的方法 |
TWI438187B (zh) | 2005-02-28 | 2014-05-21 | Evonik Degussa Gmbh | 丙烯酸和基於可再生原料之吸水聚合物結構及二者之製備方法 |
DE102005022798A1 (de) | 2005-05-12 | 2006-11-16 | Basf Ag | Verfahren zur Herstellung wenigstens eines Zielproduktes durch partielle Oxidation und/oder Ammoxidation von Propylen |
DE102005039156B4 (de) | 2005-08-17 | 2014-12-24 | Evonik Degussa Gmbh | Verfahren zur Herstellung von (Meth)Acrylsäure mit Schwersiedeaufarbeitung durch Kristallisation |
DE102005046250B4 (de) | 2005-09-27 | 2020-10-08 | Evonik Operations Gmbh | Anlage zur Abtrennung von organischen Übergangsmetallkomplexkatalysatoren |
DE102005049699A1 (de) | 2005-10-14 | 2007-04-19 | Basf Ag | Verfahren zur Herstellung von Acrolein, oder Acrylsäure oder deren Gemisch aus Propan |
US7388106B2 (en) | 2005-10-14 | 2008-06-17 | Basf Aktiengesellschaft | Process for preparing acrolein or acrylic acid or a mixture thereof from propane |
KR101278795B1 (ko) | 2005-11-03 | 2013-06-25 | 바스프 에스이 | 프로판으로부터 아크롤레인 또는 아크릴산 또는 그의혼합물을 수득하기 위한 안정한 연속 제조 방법 |
DE102005052923A1 (de) | 2005-11-03 | 2007-05-10 | Basf Ag | Verfahren zum stabilen Betreiben eines kontinuierlich ausgeübten Herstellprozesses zur Erzeugung von Acrolein, oder Acrylsäure oder deren Gemisch aus Propan |
DE102006039205A1 (de) | 2006-08-22 | 2008-03-20 | Stockhausen Gmbh | Auf nachwachsenden Rohstoffen basierende Acrylsäure und wasserabsorbierende Polymergebilde sowie Verfahren zu deren Herstellung mittels Dehydratisierung |
DE102006040430B4 (de) | 2006-08-29 | 2022-06-15 | Evonik Operations Gmbh | Verfahren zur Spaltung von MTBE |
DE102006040431A1 (de) | 2006-08-29 | 2008-03-20 | Oxeno Olefinchemie Gmbh | Verfahren zur Spaltung von MTBE |
US20080177117A1 (en) | 2006-10-16 | 2008-07-24 | Abraham Benderly | Integrated catalytic process for converting alkanes to alkenes and catalysts useful for same |
US7795469B2 (en) * | 2006-12-21 | 2010-09-14 | Rohm And Haas Company | Process for the selective (AMM) oxidation of lower molecular weight alkanes and alkenes |
DE102008020688B3 (de) | 2008-04-24 | 2009-11-05 | Evonik Stockhausen Gmbh | Verfahren zur Herstellung und Aufreinigung wässriger Phasen |
-
2008
- 2008-08-29 DE DE102008044946.6A patent/DE102008044946B4/de active Active
-
2009
- 2009-07-29 US US13/060,599 patent/US8841481B2/en active Active
- 2009-07-29 EP EP09781221.8A patent/EP2315738B1/de active Active
- 2009-07-29 JP JP2011524287A patent/JP2012500820A/ja active Pending
- 2009-07-29 BR BRPI0914143A patent/BRPI0914143A8/pt not_active IP Right Cessation
- 2009-07-29 WO PCT/EP2009/059782 patent/WO2010023053A2/de active Application Filing
- 2009-07-29 CN CN200980133421.9A patent/CN102137833B/zh active Active
-
2011
- 2011-03-25 ZA ZA2011/02225A patent/ZA201102225B/en unknown
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109789389A (zh) * | 2016-09-30 | 2019-05-21 | 赢创德固赛有限公司 | 包含金属泡沫体的固定催化床 |
CN114225848A (zh) * | 2022-02-24 | 2022-03-25 | 北京弗莱明科技有限公司 | 一种高收率连续氧化制备丁烯-2-酸的装置和方法 |
CN114225848B (zh) * | 2022-02-24 | 2022-05-13 | 北京弗莱明科技有限公司 | 一种高收率连续氧化制备丁烯-2-酸的装置和方法 |
Also Published As
Publication number | Publication date |
---|---|
JP2012500820A (ja) | 2012-01-12 |
ZA201102225B (en) | 2011-11-30 |
CN102137833B (zh) | 2014-04-16 |
US20110166304A1 (en) | 2011-07-07 |
WO2010023053A3 (de) | 2010-05-14 |
DE102008044946B4 (de) | 2022-06-15 |
US8841481B2 (en) | 2014-09-23 |
EP2315738A2 (de) | 2011-05-04 |
WO2010023053A2 (de) | 2010-03-04 |
BRPI0914143A2 (pt) | 2015-10-20 |
EP2315738B1 (de) | 2015-09-02 |
DE102008044946A1 (de) | 2010-03-04 |
BRPI0914143A8 (pt) | 2016-01-19 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN102137833B (zh) | 泡沫体在用于制备不饱和醛或羧酸的氧化反应器中的用途 | |
CN1980879B (zh) | 由丙烷生产丙烯醛、丙烯酸或其混合物的方法 | |
JP5537811B2 (ja) | 有機出発化合物の不均一系接触部分気相酸化の長期運転法 | |
US4656157A (en) | Molded catalyst for reactions carried out under heterogeneous catalysis | |
JP3150687B2 (ja) | 化学反応を行うための方法およびその反応に使用するための反応器 | |
CN101107212B (zh) | 制备不饱和脂肪酸的方法 | |
CN101300218B (zh) | 以稳定地方式操作由丙烷连续制备丙烯醛或丙烯酸或其混合物的方法的方法 | |
WO1996032188A1 (en) | Method for carrying out a chemical reaction | |
TWI302147B (en) | Method of producing unsaturated aldehyde and unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system | |
CN101287694B (zh) | 由丙烷制备丙烯醛或丙烯酸或其混合物的方法 | |
TWI288127B (en) | Method of producing unsaturated acid in fixed-bed catalytic partial oxidation reactor with enhanced heat control system | |
US6624315B2 (en) | Method of gas phase catalytic oxidation to give maleic acid anhydride | |
CN100447116C (zh) | 制备烃的至少一种部分氧化和/或氨氧化产物的方法 | |
CN101213163B (zh) | 在固定床催化部分氧化反应器中高效率制备不饱和酸的方法 | |
Liu et al. | Monolith reactor for the dehydrogenation of ethylbenzene to styrene | |
JP4456862B2 (ja) | イソ−ブタンからメタクリル酸を製造する方法 | |
JP2002507481A (ja) | 固定触媒層反応装置およびそのプロセスと産物 | |
US20040171887A1 (en) | Method for producing methacrolein from isobutane | |
CN101309889A (zh) | 由丙烷制备丙烯醛或丙烯酸或其混合物的方法 | |
Tronconi et al. | ‘High conductivity’monolith catalysts for gas/solid exothermic reactions | |
JP2009517358A (ja) | プロパンからのアクロレイン、又はアクリル酸、又はその混合物の製法 | |
CN1315819C (zh) | 马来酸酐的制备方法 | |
CN104419453B (zh) | 一种多不饱和烃选择加氢的方法 | |
CN109071393B (zh) | 不饱和醛和不饱和羧酸的制备方法 | |
CA2520832A1 (en) | In situ recoating of catalyst beds |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
ASS | Succession or assignment of patent right |
Owner name: EVONIK DEGUSSA GMBH Free format text: FORMER OWNER: EVONIK STOCKHAUSEN GMBH Effective date: 20130614 |
|
C41 | Transfer of patent application or patent right or utility model | ||
TA01 | Transfer of patent application right |
Effective date of registration: 20130614 Address after: essen Applicant after: Evonik Degussa GmbH Address before: German Clay Field Applicant before: Evonik Stockhausen GmbH |
|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder |
Address after: Essen, Germany Patentee after: Evonik Operations Limited Address before: Essen, Germany Patentee before: EVONIK DEGUSSA GmbH |
|
CP01 | Change in the name or title of a patent holder | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20211201 Address after: essen Patentee after: Evonik super absorbent Co.,Ltd. Address before: Essen Patentee before: Evonik Operations Ltd. |