WO2010058119A1 - Procede de fabrication d'un methylacrylate de methyle derive de la biomasse - Google Patents
Procede de fabrication d'un methylacrylate de methyle derive de la biomasse Download PDFInfo
- Publication number
- WO2010058119A1 WO2010058119A1 PCT/FR2009/052198 FR2009052198W WO2010058119A1 WO 2010058119 A1 WO2010058119 A1 WO 2010058119A1 FR 2009052198 W FR2009052198 W FR 2009052198W WO 2010058119 A1 WO2010058119 A1 WO 2010058119A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fraction
- methanol
- carbon monoxide
- ethanol
- reaction
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract description 38
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 32
- 239000002028 Biomass Substances 0.000 title claims abstract description 19
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 title 1
- 238000006243 chemical reaction Methods 0.000 claims abstract description 49
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 claims abstract description 37
- RJUFJBKOKNCXHH-UHFFFAOYSA-N Methyl propionate Chemical compound CCC(=O)OC RJUFJBKOKNCXHH-UHFFFAOYSA-N 0.000 claims abstract description 35
- 229940017219 methyl propionate Drugs 0.000 claims abstract description 35
- 239000000203 mixture Substances 0.000 claims abstract description 31
- NKDDWNXOKDWJAK-UHFFFAOYSA-N dimethoxymethane Chemical compound COCOC NKDDWNXOKDWJAK-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000003153 chemical reaction reagent Substances 0.000 claims abstract description 5
- REHUGJYJIZPQAV-UHFFFAOYSA-N formaldehyde;methanol Chemical compound OC.O=C REHUGJYJIZPQAV-UHFFFAOYSA-N 0.000 claims abstract description 5
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 claims abstract description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 201
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 127
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 claims description 48
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 39
- 238000003786 synthesis reaction Methods 0.000 claims description 37
- 239000007789 gas Substances 0.000 claims description 36
- 241000196324 Embryophyta Species 0.000 claims description 34
- 230000015572 biosynthetic process Effects 0.000 claims description 34
- 239000000463 material Substances 0.000 claims description 34
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 32
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 32
- 238000000855 fermentation Methods 0.000 claims description 32
- 230000004151 fermentation Effects 0.000 claims description 32
- 230000008569 process Effects 0.000 claims description 29
- 239000003054 catalyst Substances 0.000 claims description 27
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 26
- 239000005977 Ethylene Substances 0.000 claims description 26
- 239000000047 product Substances 0.000 claims description 24
- 241001465754 Metazoa Species 0.000 claims description 23
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 21
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 19
- 238000002309 gasification Methods 0.000 claims description 19
- 229910052799 carbon Inorganic materials 0.000 claims description 18
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 claims description 18
- 235000013311 vegetables Nutrition 0.000 claims description 18
- 239000001257 hydrogen Substances 0.000 claims description 16
- 229910052739 hydrogen Inorganic materials 0.000 claims description 16
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 claims description 15
- 230000018044 dehydration Effects 0.000 claims description 15
- 238000006297 dehydration reaction Methods 0.000 claims description 15
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims description 15
- 240000000111 Saccharum officinarum Species 0.000 claims description 13
- 235000007201 Saccharum officinarum Nutrition 0.000 claims description 13
- 239000002023 wood Substances 0.000 claims description 13
- 235000013339 cereals Nutrition 0.000 claims description 11
- 238000000197 pyrolysis Methods 0.000 claims description 11
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 claims description 10
- 239000006227 byproduct Substances 0.000 claims description 10
- 238000000746 purification Methods 0.000 claims description 10
- 235000019260 propionic acid Nutrition 0.000 claims description 9
- 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 claims description 9
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 claims description 8
- 239000004926 polymethyl methacrylate Substances 0.000 claims description 8
- PNEYBMLMFCGWSK-UHFFFAOYSA-N Alumina Chemical compound [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 7
- 239000000654 additive Substances 0.000 claims description 7
- 230000006315 carbonylation Effects 0.000 claims description 7
- 238000005810 carbonylation reaction Methods 0.000 claims description 7
- 230000003647 oxidation Effects 0.000 claims description 7
- 238000007254 oxidation reaction Methods 0.000 claims description 7
- 235000000346 sugar Nutrition 0.000 claims description 7
- 241000335053 Beta vulgaris Species 0.000 claims description 6
- 244000061456 Solanum tuberosum Species 0.000 claims description 6
- 235000002595 Solanum tuberosum Nutrition 0.000 claims description 6
- 239000001913 cellulose Substances 0.000 claims description 6
- 229920002678 cellulose Polymers 0.000 claims description 6
- 230000032050 esterification Effects 0.000 claims description 6
- 238000005886 esterification reaction Methods 0.000 claims description 6
- 238000005984 hydrogenation reaction Methods 0.000 claims description 6
- 238000006460 hydrolysis reaction Methods 0.000 claims description 6
- 229920003229 poly(methyl methacrylate) Polymers 0.000 claims description 6
- 150000003626 triacylglycerols Chemical class 0.000 claims description 6
- 239000004925 Acrylic resin Substances 0.000 claims description 5
- 229920000178 Acrylic resin Polymers 0.000 claims description 5
- 240000002791 Brassica napus Species 0.000 claims description 5
- 235000004977 Brassica sinapistrum Nutrition 0.000 claims description 5
- 235000010469 Glycine max Nutrition 0.000 claims description 5
- 244000020551 Helianthus annuus Species 0.000 claims description 5
- 235000003222 Helianthus annuus Nutrition 0.000 claims description 5
- 229920002472 Starch Polymers 0.000 claims description 5
- 230000000996 additive effect Effects 0.000 claims description 5
- 229920001577 copolymer Polymers 0.000 claims description 5
- 239000000839 emulsion Substances 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 5
- 239000008107 starch Substances 0.000 claims description 5
- 235000019698 starch Nutrition 0.000 claims description 5
- 239000007858 starting material Substances 0.000 claims description 5
- 238000005809 transesterification reaction Methods 0.000 claims description 5
- 239000002699 waste material Substances 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 239000002551 biofuel Substances 0.000 claims description 4
- 230000007062 hydrolysis Effects 0.000 claims description 4
- 150000002734 metacrylic acid derivatives Chemical class 0.000 claims description 4
- 239000000178 monomer Substances 0.000 claims description 4
- 239000004800 polyvinyl chloride Substances 0.000 claims description 4
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 4
- 238000004061 bleaching Methods 0.000 claims description 3
- 235000014113 dietary fatty acids Nutrition 0.000 claims description 3
- 229930195729 fatty acid Natural products 0.000 claims description 3
- 239000000194 fatty acid Substances 0.000 claims description 3
- 150000004665 fatty acids Chemical class 0.000 claims description 3
- 150000002194 fatty esters Chemical class 0.000 claims description 3
- 239000000314 lubricant Substances 0.000 claims description 3
- 238000006063 methoxycarbonylation reaction Methods 0.000 claims description 3
- 239000000419 plant extract Substances 0.000 claims description 3
- 235000012015 potatoes Nutrition 0.000 claims description 3
- 150000008163 sugars Chemical class 0.000 claims description 3
- 235000016068 Berberis vulgaris Nutrition 0.000 claims description 2
- 239000010815 organic waste Substances 0.000 claims description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 30
- 229960004279 formaldehyde Drugs 0.000 description 18
- 229910002092 carbon dioxide Inorganic materials 0.000 description 16
- 239000001569 carbon dioxide Substances 0.000 description 15
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 14
- 239000002994 raw material Substances 0.000 description 14
- 240000008042 Zea mays Species 0.000 description 13
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 13
- 241000209140 Triticum Species 0.000 description 12
- 235000021307 Triticum Nutrition 0.000 description 12
- 235000019256 formaldehyde Nutrition 0.000 description 12
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 10
- 235000005822 corn Nutrition 0.000 description 10
- 240000004808 Saccharomyces cerevisiae Species 0.000 description 9
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 9
- 239000000523 sample Substances 0.000 description 9
- 235000014680 Saccharomyces cerevisiae Nutrition 0.000 description 8
- 230000003197 catalytic effect Effects 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 6
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 6
- 239000012535 impurity Substances 0.000 description 6
- 239000003921 oil Substances 0.000 description 6
- 235000019198 oils Nutrition 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 125000004432 carbon atom Chemical group C* 0.000 description 5
- 238000004821 distillation Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 229910052760 oxygen Inorganic materials 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000010936 titanium Substances 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 235000021536 Sugar beet Nutrition 0.000 description 4
- QCWXUUIWCKQGHC-UHFFFAOYSA-N Zirconium Chemical compound [Zr] QCWXUUIWCKQGHC-UHFFFAOYSA-N 0.000 description 4
- 150000001298 alcohols Chemical class 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- TZIHFWKZFHZASV-UHFFFAOYSA-N methyl formate Chemical compound COC=O TZIHFWKZFHZASV-UHFFFAOYSA-N 0.000 description 4
- 239000000377 silicon dioxide Substances 0.000 description 4
- 239000000243 solution Substances 0.000 description 4
- 229910052726 zirconium Inorganic materials 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- 235000021537 Beetroot Nutrition 0.000 description 3
- 229920002488 Hemicellulose Polymers 0.000 description 3
- 240000005979 Hordeum vulgare Species 0.000 description 3
- 235000007340 Hordeum vulgare Nutrition 0.000 description 3
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 3
- 240000006394 Sorghum bicolor Species 0.000 description 3
- 235000011684 Sorghum saccharatum Nutrition 0.000 description 3
- 235000016383 Zea mays subsp huehuetenangensis Nutrition 0.000 description 3
- 229910052792 caesium Inorganic materials 0.000 description 3
- TVFDJXOCXUVLDH-UHFFFAOYSA-N caesium atom Chemical compound [Cs] TVFDJXOCXUVLDH-UHFFFAOYSA-N 0.000 description 3
- 239000003245 coal Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000001307 helium Substances 0.000 description 3
- 229910052734 helium Inorganic materials 0.000 description 3
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 3
- 229920005610 lignin Polymers 0.000 description 3
- 235000009973 maize Nutrition 0.000 description 3
- 239000002808 molecular sieve Substances 0.000 description 3
- 229910052763 palladium Inorganic materials 0.000 description 3
- 230000002285 radioactive effect Effects 0.000 description 3
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 3
- 239000010902 straw Substances 0.000 description 3
- ZSLUVFAKFWKJRC-IGMARMGPSA-N 232Th Chemical compound [232Th] ZSLUVFAKFWKJRC-IGMARMGPSA-N 0.000 description 2
- HGINCPLSRVDWNT-UHFFFAOYSA-N Acrolein Chemical compound C=CC=O HGINCPLSRVDWNT-UHFFFAOYSA-N 0.000 description 2
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 description 2
- 241000283073 Equus caballus Species 0.000 description 2
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 description 2
- NBBJYMSMWIIQGU-UHFFFAOYSA-N Propionic aldehyde Chemical compound CCC=O NBBJYMSMWIIQGU-UHFFFAOYSA-N 0.000 description 2
- WQDUMFSSJAZKTM-UHFFFAOYSA-N Sodium methoxide Chemical compound [Na+].[O-]C WQDUMFSSJAZKTM-UHFFFAOYSA-N 0.000 description 2
- 229910052776 Thorium Inorganic materials 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 2
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 125000004429 atom Chemical group 0.000 description 2
- 239000006229 carbon black Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000003925 fat Substances 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- 239000008103 glucose Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 229940003953 helium / oxygen Drugs 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- PHTQWCKDNZKARW-UHFFFAOYSA-N isoamylol Chemical compound CC(C)CCO PHTQWCKDNZKARW-UHFFFAOYSA-N 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 238000004949 mass spectrometry Methods 0.000 description 2
- 235000013379 molasses Nutrition 0.000 description 2
- 235000014593 oils and fats Nutrition 0.000 description 2
- 239000003209 petroleum derivative Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 229920005989 resin Polymers 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
- 239000002002 slurry Substances 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910052719 titanium Inorganic materials 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- OERNJTNJEZOPIA-UHFFFAOYSA-N zirconium nitrate Chemical compound [Zr+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O OERNJTNJEZOPIA-UHFFFAOYSA-N 0.000 description 2
- 229920005440 Altuglas® Polymers 0.000 description 1
- 229910018516 Al—O Inorganic materials 0.000 description 1
- 241000283690 Bos taurus Species 0.000 description 1
- ZWYHROJOZRUXFM-UHFFFAOYSA-N C(C1=CC=CC=C1)=CC(=O)C=CC1=CC=CC=C1.C(C)(C)(C)P(C(C)(C)C)C1=C(C(=CC=C1)C)C Chemical compound C(C1=CC=CC=C1)=CC(=O)C=CC1=CC=CC=C1.C(C)(C)(C)P(C(C)(C)C)C1=C(C(=CC=C1)C)C ZWYHROJOZRUXFM-UHFFFAOYSA-N 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241000283707 Capra Species 0.000 description 1
- OKTJSMMVPCPJKN-NJFSPNSNSA-N Carbon-14 Chemical compound [14C] OKTJSMMVPCPJKN-NJFSPNSNSA-N 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-L Carbonate Chemical compound [O-]C([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-L 0.000 description 1
- 241000252203 Clupea harengus Species 0.000 description 1
- 241001481833 Coryphaena hippurus Species 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 240000008892 Helianthus tuberosus Species 0.000 description 1
- 235000003230 Helianthus tuberosus Nutrition 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- FYYHWMGAXLPEAU-UHFFFAOYSA-N Magnesium Chemical compound [Mg] FYYHWMGAXLPEAU-UHFFFAOYSA-N 0.000 description 1
- AFCARXCZXQIEQB-UHFFFAOYSA-N N-[3-oxo-3-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)propyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CCNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 AFCARXCZXQIEQB-UHFFFAOYSA-N 0.000 description 1
- 229910002651 NO3 Inorganic materials 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- 229910019142 PO4 Inorganic materials 0.000 description 1
- 241000283222 Physeter catodon Species 0.000 description 1
- 240000004713 Pisum sativum Species 0.000 description 1
- 235000010582 Pisum sativum Nutrition 0.000 description 1
- 229920005372 Plexiglas® Polymers 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 241001125046 Sardina pilchardus Species 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- 229910006367 Si—P Inorganic materials 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- 229930006000 Sucrose Natural products 0.000 description 1
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 1
- 241000282887 Suidae Species 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 229910000323 aluminium silicate Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 235000015241 bacon Nutrition 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 150000007514 bases Chemical class 0.000 description 1
- 235000015278 beef Nutrition 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 description 1
- 239000004327 boric acid Substances 0.000 description 1
- 230000005587 bubbling Effects 0.000 description 1
- ZTQSAGDEMFDKMZ-UHFFFAOYSA-N butyric aldehyde Natural products CCCC=O ZTQSAGDEMFDKMZ-UHFFFAOYSA-N 0.000 description 1
- FJDQFPXHSGXQBY-UHFFFAOYSA-L caesium carbonate Chemical compound [Cs+].[Cs+].[O-]C([O-])=O FJDQFPXHSGXQBY-UHFFFAOYSA-L 0.000 description 1
- 229910000024 caesium carbonate Inorganic materials 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 235000013330 chicken meat Nutrition 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- 239000003026 cod liver oil Substances 0.000 description 1
- 235000012716 cod liver oil Nutrition 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010790 dilution Methods 0.000 description 1
- 239000012895 dilution Substances 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 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
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229940013317 fish oils Drugs 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000008246 gaseous mixture Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000010439 graphite Substances 0.000 description 1
- 229910002804 graphite Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 150000002373 hemiacetals Chemical class 0.000 description 1
- 235000019514 herring Nutrition 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000000976 ink Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 229910052747 lanthanoid Inorganic materials 0.000 description 1
- 150000002602 lanthanoids Chemical class 0.000 description 1
- 239000003879 lubricant additive Substances 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 230000004060 metabolic process Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229940098779 methanesulfonic acid Drugs 0.000 description 1
- SICCRERQCOIGDC-UHFFFAOYSA-N methanol;methyl propanoate Chemical compound OC.CCC(=O)OC SICCRERQCOIGDC-UHFFFAOYSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 235000021243 milk fat Nutrition 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- MEFBJEMVZONFCJ-UHFFFAOYSA-N molybdate Chemical compound [O-][Mo]([O-])(=O)=O MEFBJEMVZONFCJ-UHFFFAOYSA-N 0.000 description 1
- 239000003345 natural gas Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000000123 paper Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 235000021317 phosphate Nutrition 0.000 description 1
- 150000003013 phosphoric acid derivatives Chemical class 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920006324 polyoxymethylene Polymers 0.000 description 1
- 235000015277 pork Nutrition 0.000 description 1
- 235000021395 porridge Nutrition 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000012429 reaction media Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000013074 reference sample Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 230000004044 response Effects 0.000 description 1
- 235000019512 sardine Nutrition 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- 150000004760 silicates Chemical class 0.000 description 1
- GCLGEJMYGQKIIW-UHFFFAOYSA-H sodium hexametaphosphate Chemical compound [Na]OP1(=O)OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])OP(=O)(O[Na])O1 GCLGEJMYGQKIIW-UHFFFAOYSA-H 0.000 description 1
- 239000011949 solid catalyst Substances 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000004611 spectroscopical analysis Methods 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 239000005720 sucrose Substances 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 239000003760 tallow Substances 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
- 239000006200 vaporizer Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
- 239000010698 whale oil Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/30—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
- C07C67/303—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by hydrogenation of unsaturated carbon-to-carbon bonds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
- C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/15—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively
- C07C29/151—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of oxides of carbon exclusively with hydrogen or hydrogen-containing gases
- C07C29/1516—Multisteps
- C07C29/1518—Multisteps one step being the formation of initial mixture of carbon oxides and hydrogen for synthesis
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C41/00—Preparation of ethers; Preparation of compounds having groups, groups or groups
- C07C41/48—Preparation of compounds having groups
- C07C41/50—Preparation of compounds having groups by reactions producing groups
-
- 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
- C07C45/49—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide
- C07C45/50—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by reaction with carbon monoxide by oxo-reactions
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/08—Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/30—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group
- C07C67/333—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton
- C07C67/343—Preparation of carboxylic acid esters by modifying the acid moiety of the ester, such modification not being an introduction of an ester group by isomerisation; by change of size of the carbon skeleton by increase in the number of carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C67/00—Preparation of carboxylic acid esters
- C07C67/36—Preparation of carboxylic acid esters by reaction with carbon monoxide or formates
- C07C67/38—Preparation of carboxylic acid esters by reaction with carbon monoxide or formates by addition to an unsaturated carbon-to-carbon bond
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F20/00—Homopolymers and copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical or a salt, anhydride, ester, amide, imide or nitrile thereof
- C08F20/02—Monocarboxylic acids having less than ten carbon atoms, Derivatives thereof
- C08F20/10—Esters
- C08F20/12—Esters of monohydric alcohols or phenols
- C08F20/14—Methyl esters, e.g. methyl (meth)acrylate
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M145/00—Lubricating compositions characterised by the additive being a macromolecular compound containing oxygen
- C10M145/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M145/10—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate
- C10M145/12—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate monocarboxylic
- C10M145/14—Acrylate; Methacrylate
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11C—FATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
- C11C3/00—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
- C11C3/04—Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
-
- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
- C12P7/00—Preparation of oxygen-containing organic compounds
- C12P7/62—Carboxylic acid esters
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/02—Boron or aluminium; Oxides or hydroxides thereof
- C07C2521/04—Alumina
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M2209/00—Organic macromolecular compounds containing oxygen as ingredients in lubricant compositions
- C10M2209/02—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C10M2209/08—Macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing monomers having an unsaturated radical bound to a carboxyl radical, e.g. acrylate type
- C10M2209/084—Acrylate; Methacrylate
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/10—Biofuels, e.g. bio-diesel
-
- 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
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Definitions
- the present invention relates to a process for producing a methyl methacrylate derived from biomass.
- Methyl methacrylate is the starting material for many polymerization or copolymerization reactions.
- PMMA poly (methyl methacrylate)
- ALTUGLAS ® and PLEXIGLAS ® poly (methyl methacrylate)
- PLEXIGLAS ® poly (methyl methacrylate)
- It is in the form of powders, granules or plates, the powders or granules used to mold various articles, such as articles for the automobile, household and office items, and the plates found use in the signs and displays, in the fields of transportation, building, lighting and sanitary, as noise barriers, for works of art, flat screens, etc.
- Methyl methacrylate is also the starting material for the organic synthesis of higher methacrylates, which, like it, are used in the preparation of acrylic emulsions and acrylic resins, serve as additives for polyvinyl chloride, enter As comonomers in the manufacture of many copolymers such as methyl methacrylate-butadiene-styrene copolymers, serve as additives for lubricants, and have many other applications among which one could mention medical prostheses, flocculants, products of maintenance, etc.
- Acrylic emulsions and resins have applications in the fields of paints, adhesives, paper, textiles, inks, etc.
- Acrylic resins serve also in the manufacture of plates, having the same applications as the PMMA.
- Methyl methacrylate can be obtained in a variety of ways, one of which is an alpha addition of formaldehyde to methyl propionate, depending on the reaction:
- Methyl methacrylate can also be obtained by reacting methyl propionate with a formaldehyde-methanol mixture or with methylal
- Methyl propionate can be obtained by carbonylation of ethylene in the presence of methanol, by esterification of propionic acid with methanol or by hydrogenation of methyl acrylate.
- Propionic acid can be obtained by carbonylation of ethanol or by hydrogenation of acrylic acid.
- Methyl acrylate can be obtained by esterification of acrylic acid with methanol.
- the acrylic acid can be obtained by oxidation of acrolein, which can be obtained by catalytic oxidation of propylene or by dehydration of glycerol, obtaining acrylic acid as a by-product.
- the raw materials used for these syntheses of methyl methacrylate are mainly of petroleum origin or of synthetic origin, comprising Many sources of CO2 emissions contribute to the increase of the greenhouse effect.
- the raw materials used for these syntheses of methyl methacrylate are mainly of petroleum origin or of synthetic origin, comprising Many sources of CO2 emissions contribute to the increase of the greenhouse effect.
- it is a question of manufacturing methyl methacrylate by reaction of methyl propionate with formaldehyde the methyl propionate having been obtained by reaction of methoxycarbonylation of ethylene with carbon monoxide from a synthesis gas derived from coal (coal of fossil origin).
- the source of these raw materials will gradually run out.
- Raw materials from biomass are renewable and have a reduced impact on the environment. They do not require all the refining steps, very expensive in energy, petroleum products.
- the production of fossil CO2 is reduced so that they contribute less to global warming.
- the plant has consumed atmospheric CO2 at a rate of 44g of CO2 per mole of carbon (or for 12 g of carbon). So the use of a renewable source begins by decreasing the amount of atmospheric CO2.
- the vegetable matter has the advantage of being able to be cultivated in large quantity, according to the demand, on most of the terrestrial globe.
- Biomass is the raw material of plant or animal origin naturally produced. This plant material is characterized by the fact that the plant for its growth has consumed atmospheric CO2 while producing oxygen. The animals for their growth consumed this vegetable raw material and thus assimilated carbon derived from atmospheric CO2.
- the purpose of the present invention is therefore to respond to certain concerns of sustainable development.
- the subject of the present invention is therefore a process for producing methyl methacrylate by reacting methyl propionate with formaldehyde or a formaldehyde-methanol or methylal mixture, characterized in that at least a fraction of at least one reagent involved in this reaction was obtained by a reaction or a succession of reactions from the biomass.
- the reaction of methyl propionate with formaldehyde consists of a catalytic condensation in the gas phase, with a large excess of methyl propionate, optionally in the presence of methanol, at a temperature generally between 225 ° C. and 450 ° C.
- the catalysts alkali or alkaline-earth metal aluminosilicates, silica or alumina impregnated with a hydroxide, a carbonate or a nitrate, for example potassium, cesium or zirconium, or a lanthanide. Operating conditions for carrying out the reaction are described in particular in documents FR 2 223 080 or US Pat. No. 3,701,798.
- the reaction of methyl propionate with methylal is carried out with an excess of methyl propionate, optionally in the presence of water, at a temperature generally of between 200 ° C. and 500 ° C. in the presence of a catalyst which may be chosen from phosphates and / or silicates of magnesium, calcium, aluminum, zirconium, thorium, and / or titanium, alone or with the addition of oxides of zirconium, aluminum, thorium and / or titanium and and / or boric acid and / or urea, the catalyst being capable of being modified with an alkaline or alkaline-earth carboxylate.
- a catalyst which may be chosen from phosphates and / or silicates of magnesium, calcium, aluminum, zirconium, thorium, and / or titanium, alone or with the addition of oxides of zirconium, aluminum, thorium and / or titanium and and / or boric acid and / or urea, the catalyst being capable of being modified with
- At least one fraction of methyl propionate can be obtained by carbonylation of ethylene in the presence of methanol, at least a fraction of at least one of ethylene, carbon and methanol involved in this methoxycarbonylation reaction having been obtained by a reaction or a succession of reactions from the biomass.
- At least one fraction of ethylene may be obtained by ethanol synthesis by ethanol fermentation of at least one plant material and optionally purification of the ethanol obtained, then by dehydration of the ethanol obtained to produce a mixture of ethylene and water, removal of water and optionally purification of the ethylene obtained; and / or having obtained at least a fraction of the carbon monoxide by gasification of any material of animal or vegetable origin, leading to a synthesis gas consisting essentially of carbon monoxide and hydrogen, from which carbon monoxide has been extracted ; and / or having obtained at least a fraction of the methanol by pyrolysis of the wood or by gasification of any material of animal or vegetable origin leading to a synthesis gas consisting essentially of carbon monoxide and hydrogen, or by fermentation from plant crops such as wheat, corn, sugar cane or beetroot, giving fermentable products and therefore alcohol.
- plant crops such as wheat, corn, sugar cane or beetroot
- the plant material subjected to the ethanolic fermentation may advantageously have been chosen from sugars, starch and plant extracts containing thereof, among which mention may be made of beetroot, sugar cane, cereals such as corn, wheat , barley and sorghum, potatoes, and a source of cellulose (mixture of cellulose, hemicellulose and lignin), but also organic waste.
- the fermentation is then obtained, for example using Saccharomyces cerevisiae or its mutant, ethanol.
- the dehydration of ethanol could have been carried out using a catalyst based on ⁇ -alumina.
- At least one fraction of methyl propionate can be obtained by esterification of propionic acid with methanol, at least a fraction of at least one of the acid propionic and methanol put in in this reaction having been obtained by a reaction or a succession of reactions from the biomass.
- At least a fraction of the propionic acid can be obtained by carbonylation of the ethanol, at least a fraction of the carbon monoxide having been obtained by gasification of all materials of animal or vegetable origin, leading to a gas synthesis compound consisting essentially of carbon monoxide and hydrogen, from which carbon monoxide has been extracted; and at least a fraction of the ethanol obtained by fermentation of at least one plant material and optionally purification of the ethanol obtained; and / or at least one fraction of methanol can be obtained by pyrolysis of the wood or by gasification of any material of animal or vegetable origin leading to a synthesis gas consisting essentially of carbon monoxide and hydrogen, or by fermentation at from plant crops such as wheat, corn, sugar cane or beetroot, giving fermentable products and therefore alcohol.
- At least a fraction of the propionic acid may also have been obtained by hydrogenation of acrylic acid, which has been obtained as a by-product of the dehydration of glycerol. It has been possible to obtain at least a fraction of glycerol as a by-product of the manufacture of biofuels from oleaginous plants such as rapeseed, sunflower or soy containing triglycerides, hydrolysis or transesterification of these triglycerides to form glycerol apart from fatty acids and fatty esters respectively.
- a third embodiment of the invention it has been possible to obtain at least a fraction of the methyl propionate by hydrogenation of methyl acrylate, itself obtained by esterification of acrylic acid with methanol, at least a fraction of the methanol having been obtained by pyrolysis of the wood or by gasification of all materials of animal origin or vegetable leading to a synthesis gas composed essentially of carbon monoxide and hydrogen, or by fermentation from crops of plants such as wheat, corn, sugar cane or beet, giving fermentable products and therefore of the alcohol ; and / or at least a fraction of the acrylic acid which has been obtained as a by-product of the dehydration of glycerol, itself obtained as a by-product of the production of biofuels from oleaginous plants such as rapeseed, sunflower or soy.
- the synthesis gas for preparing the methanol advantageously comes from the waste liquor of the manufacture and bleaching of cellulosic pulps.
- the subject of the present invention is also the use of methyl methacrylate manufactured by the process as defined above, as monomer for the manufacture of poly (methyl methacrylate), as starting material for the organic synthesis of methacrylates. as a product used in the preparation of acrylic emulsions and acrylic resins, as an additive for polyvinyl chloride, as a comonomer in the manufacture of copolymers and as a lubricant additive.
- methanol is obtained by pyrolysis of the wood, by gasification of all materials of animal or vegetable origin, leading to a synthesis gas composed essentially of carbon monoxide and hydrogen which is optionally reacted. with water in order to adjust the H 2 / CO ratio in the proportions appropriate to the synthesis of methanol, or by fermentation from crops of plants such as wheat, corn, sugar cane or beet, giving fermentable products and therefore alcohol.
- the materials of animal origin are, by way of non-limiting examples, fish oils and fats, such as cod liver oil, whale oil, sperm whale, dolphin oil, seal oil, sardine oil, herring oil, squales, oils and fats of cattle, pigs, goats, equines, and poultry, such as tallow, lard, milk fat, bacon, chicken fat, beef, pork, horse, and others.
- fish oils and fats such as cod liver oil, whale oil, sperm whale, dolphin oil, seal oil, sardine oil, herring oil, squales, oils and fats of cattle, pigs, goats, equines, and poultry, such as tallow, lard, milk fat, bacon, chicken fat, beef, pork, horse, and others.
- Plant-based materials are, by way of non-limiting examples, ligno-cellulosic residues from agriculture, cereal straw fodder, such as wheat straw, straw or maize residues; cereal residues as maize residues; cereal flours, such as wheat flour; cereals such as wheat, barley, sorghum, maize; wood, waste and scrap wood; grains; sugar cane, sugar cane residues; shoots and stems of peas; beetroot, molasses such as beet molasses; Jerusalem artichokes; potatoes, potato tops, potato residues; starch; mixtures of cellulose, hemicellulose and lignin, and the black liquor of stationery, which is a carbon-rich material.
- the synthesis gas for preparing methanol comes from the recovery of waste liquor from the manufacture of cellulosic pulps.
- Ethylene is obtained by dehydration of ethanol, which is obtained by ethanolic fermentation of at least one plant material, in the presence of one or more yeasts or mutants of these yeasts.
- the plant material may especially be chosen from sugars, starch and plant extracts containing it, among which include beetroot, sugar cane, cereals such as wheat, barley, sorghum or wheat. corn, as well as the potato, without this list being exhaustive. It can alternatively be biomass (mixture of cellulose, hemicellulose and lignin).
- the plant material used is generally in hydrolysed form before the fermentation stage.
- This preliminary hydrolysis step thus allows, for example, the saccharification of starch to transform it into glucose, or the transformation of sucrose into glucose.
- Ethanol is generally obtained in mixture with heavier alcohols, called Fusel alcohols, the composition of which depends on the plant material used and the fermentation process. These generally comprise about 50% of iso-amyl alcohol (C5) and some percentages of C3 and C4 alcohols (isobutanol).
- Fusel alcohols the composition of which depends on the plant material used and the fermentation process.
- These generally comprise about 50% of iso-amyl alcohol (C5) and some percentages of C3 and C4 alcohols (isobutanol).
- it is therefore preferable to purify the ethanol produced by fermentation for example by distillation and / or absorption on filters of the molecular sieve, carbon black or zeolite type.
- the ethanol obtained by fermentation and advantageously purified as indicated above is then dehydrated in a reactor in a mixture of ethylene and water. It is preferred that the ethanol is injected at the top of the reactor.
- This dehydration step is generally conducted in the presence of a catalyst which may be a ⁇ -alumina.
- a catalyst suitable for the dehydration of ethanol is especially marketed by the company EUROSUPPORT under the trade name ESM 110 ® . It is an undoped trilobal alumina containing little residual Na2 ⁇ 0 (usually 0.04%). Those skilled in the art will be able to choose the optimal operating conditions for this dehydration step.
- the ethylene obtained may optionally be constituted by a mixture with other alkenes if there has been no purification of ethanol as indicated above, that is, if the ethanol has been subjected to dehydration in mixed with Fusel alcohols. It is therefore advantageous in this case to provide a step of purifying the ethylene obtained, for example by absorption on molecular sieve type filters, carbon black or zeolites.
- Carbon monoxide is obtained by gasification of all materials of animal or vegetable origin, leading to a synthesis gas composed essentially of carbon monoxide and hydrogen, from which carbon monoxide is extracted.
- Glycerol is obtained from oleaginous plants such as rapeseed, sunflower or soya, containing oils (triglycerides) or animal fats.
- a step of hydrolysis or transesterification of triglycerides is carried out to form, with glycerol, respectively fatty acids or fatty esters.
- this transesterification can be carried out by reacting the crude oil in a stirred reactor in the presence of an excess of alcohol (for example methanol), preferably with a basic catalyst
- the crude oil is reacted in the presence of an excess of water, preferably with an acid catalyst.
- This transesterification or hydrolysis reaction is preferably carried out at a temperature of between 40 and 120 ° C.
- the reactor is continuously fed to maintain the water / acid or alcohol / ester molar ratio of greater than or equal to 2. 1.
- the glycerol is separated from the mixture obtained by decantation.
- the present invention thus makes it possible to obtain a methyl methacrylate having at least a portion of its carbons of renewable origin.
- a renewable raw material, or bioressourcée is a natural resource, animal or vegetable, whose stock can be reconstituted over a short period on a human scale. In particular, this stock must be renewed as quickly as it is consumed.
- renewable raw materials contain 14 C in the same proportions as atmospheric CO2. All carbon samples from living organisms
- the 14 C / 12 C ratio of living tissues is identical to that of the atmosphere.
- 14 C exists in two main forms: in mineral form, that is to say carbon dioxide (CO2), and in organic form, that is to say carbon incorporated into molecules
- CO2 carbon dioxide
- organic form that is to say carbon incorporated into molecules
- the 14 C / 12 C ratio is kept constant by the metabolism because the carbon is continuously exchanged with the environment, the proportion of 14 C being constant in the atmosphere, the same is true in the organism, as long as it is alive, since it absorbs this 14 C as it absorbs 12 C.
- the average ratio of 14 C / 12 C is equal to l, 2xl ⁇ ⁇ 12 for a bioresourced material, while carbon 14 is derived from the bombardment of atmospheric nitrogen (14), and spontaneously oxidizes with the oxygen of the In our human history, the content of 14 C02 has increased as a result of atmospheric nuclear explosions, and has steadily decreased after stopping these tests.
- 12 C is stable, that is to say that the number of atoms of 12 C in a given sample is constant over time.
- 14 C is radioactive (each gram of carbon in a living being contains enough 14 C isotopes to give 13.6 disintegrations per minute) and the number of such atoms in a sample decreases over time (t ) according to the law :
- - no is the number of 14 C at the origin (on the death of the creature, animal or plant),
- n is the number of 14 C atoms remaining at the end of time t
- - at. is the disintegration constant (or radioactive constant); it is connected to the half-life.
- the half-life of 14 C is 5730 years. In 50 000 years the 14 C content is less than 0.2% of the initial content and therefore becomes difficult to detect. Petroleum products, or natural gas or coal therefore do not contain 14 C.
- the 14 C content is substantially constant from the extraction of renewable raw materials, to the manufacture of methyl methacrylate 1 according to the invention and even up at the end of its use.
- the methyl methacrylate obtained according to the invention contains organic carbon derived from renewable raw materials; it is therefore characterized in that it contains 14 C.
- At least 1% by weight of the carbon atoms of said methyl methacrylate is of renewable origin.
- at least 20% of the carbons of said methyl methacrylate are of renewable origin.
- at least 40% of the carbons of said methyl methacrylate are of renewable origin.
- at least 60%, and even more at least 80% of the carbon atoms of said methyl methacrylate are of renewable origin.
- the methyl methacrylate obtained according to the invention contains at least 0.01 ⁇ 10 -10 % by weight, preferably at least 0.2 ⁇ 10 -10 %, of 14 C relative to the total mass of carbon. Even more preferably, said methyl methacrylate contains at least 0.4 ⁇ 10 -10 % of 14 C, more particularly at least 0.7 ⁇ 10 -10 % of 14 C, and even more specifically at least 0.9 ⁇ 10 -10 %. 14 C.
- methyl methacrylate obtained by the process according to the invention contains 0,2xl0 ⁇ 10% when, 2xl ⁇ ⁇ 10% by mass
- the methyl methacrylate obtained according to the invention contains 100% organic carbon derived from renewable raw materials and therefore 1, 2xl ⁇ ⁇ 10
- the 14 C content of methyl methacrylate can be measured for example according to the following techniques: by liquid scintillation spectrometry: this method consists in counting 'Beta' particles resulting from the decay of 14 C. The radiation is measured
- Beta from a sample of known mass (number of known carbon atoms) for a certain time. This 'radioactivity' is proportional to the number of 14 C atoms, which can be determined.
- the 14 C present in the sample emits ⁇ - radiation, which, in contact with the scintillating liquid (scintillator), give rise to photons. These photons have different energies (between 0 and 156 Kev) and form what we call a spectrum of 14 C.
- the analysis relates to the CO2 previously produced by combustion of the carbon sample in an appropriate absorbent solution, or on benzene after prior conversion of the carbon sample to benzene, by mass spectrometry: the sample is reduced to graphite or gaseous CO2, analyzed in a mass spectrometer.
- This technique uses an accelerator and a mass spectrometer to separate 14 C ions and 12 C and thus determine the ratio of the two isotopes.
- the measurement method preferably used in the case of methyl methacrylate is the mass spectrometry described in ASTM D6866-06.
- the methyl methacrylate obtained according to the process according to the invention constitutes a raw material containing mainly methyl methacrylate, in the sense that the product resulting from the process may comprise impurities related to the nature of the reagents used or generated during the course of the process. process, which may be different from the impurities generated during the implementation of reagents of fossil origin.
- the method according to the invention may therefore further comprise one or more purification steps.
- the methyl methacrylate obtained according to the process according to the invention can be used as it is or optionally after a purification step, such as raw material in all the applications in which it is known to use MAM, especially as monomer for the manufacture of poly (methyl methacrylate), as a starting material for the organic synthesis of higher methacrylates, as a product used in the preparation of acrylic emulsions and acrylic resins, as additive for polyvinyl chloride, as comonomer in the manufacture of copolymers and as additive for lubricants.
- MAM monomer for the manufacture of poly (methyl methacrylate)
- a starting material for the organic synthesis of higher methacrylates as a product used in the preparation of acrylic emulsions and acrylic resins
- additive for polyvinyl chloride as comonomer in the manufacture of copolymers and as additive for lubricants.
- Example 1 Manufacture of methyl methacrylate by reaction of methyl propionate with a formaldehyde-methanol mixture
- a water-sugar mixture (10 kg of sugar) is poured into a 50-liter plastic tank. 0.25 l of baker's yeast mixed beforehand with 0.25 l of warm water, a dose of Calgon (water softener) are added to the mixture and the mixture is left to macerate for 14 days at a temperature of 25 ° C. To limit the formation of acetic acid, the container is covered with a lid provided with a valve. At the end of this step, the mixture is filtered, decanted and the solution is distilled to recover the azeotrope of ethanol, 96% in water.
- Calgon water softener
- Corn kernels are used in a container and covered with hot water. Tissue is placed over the container to limit contamination and heat loss. The container is provided with a hole in the foot to allow a slow flow. Hot water is added regularly to maintain the level. The container is thus maintained for 3 days or until the grains have sufficiently exploded. Then the grains are dried and ground.
- a slurry is prepared by adding hot water, and thus maintained to start the fermentation.
- a yeast is added for the fermentation (250 g of yeast for 200 liters of slurry for example), and optionally sugar. With yeast, the fermentation takes about 3 days, in the absence of yeast it can take 10 days.
- a yeast Saccharomyces cerevisiae is used. The porridge is converted when it stops bubbling. Fermentation produces both ethanol and CO2. The product is placed in a boiler equipped with a distillation column. The first distilled fractions contain volatile contaminants and alcohol, and are removed. Then the ethanol is collected. The last fractions are low in alcohol.
- Ib - Manufacture of ethylene by dehydration of ethanol 96% ethanol, obtained by ethanol fermentation of corn or sugar grains as described previously, is vaporized in a vaporizer, then preheated in a heat exchanger, before being injected at the head of a 127 mm diameter reactor containing a catalytic bed heated to 300-400 0 C and consisting of a layer of alumina ESM110 ® EUROSUPPORT, representing a volume of 12700cm 3 and a mass of 6500 g, the ratio of the volume flow rate of ethanol to the catalyst volume being Ih "1.
- the mixture of water and ethylene produced in the reactor is cooled in the heat exchanger, before being sent to a gas-liquid separator where ethylene and water (possibly mixed with by-products) are separated.
- a solid catalyst based on palladium palladium (di-t-butylphosphino o-xylene) dibenzylidene acetone (37 mg, 5.0 * 10 -5 mole), cobalt carbonyl (9 mg, 2.6 * 10 -5 mole) and methanesulfonic acid produced by Arkema (68 microliters, 1.0 * 10 -3 mol) are dissolved in methanol (219 ml, 5.41 mol) and methyl propionate (81 ml, 0.841 mol) under an atmosphere. nitrogen.
- the solution is transferred to an autoclave and heated to 80 ° C., and then CO and the ethylene prepared above in a molar ratio of 1: 1 are introduced into the reactor continuously at a total pressure of 10 bar.
- the reaction is carried out for a period of 4 hours and the products are analyzed to determine the amount of methyl propionate formed: 4329 kg of methyl propionate per kg of palladium per hour.
- the yield of the reaction relative to the methanol involved is 19%.
- unconverted ethylene and CO are recycled, and the methanol remains in the reactor.
- the methyl propionate is then isolated for the next step.
- a Cs / Zr / SiO 2 type catalyst prepared from a silica gel in the form of 2-4 mm diameter spheres having a purity of 99.9% and a surface area of 320 m is used. 2 / g and a pore volume of 0.83 cm 3 / g with a median pore diameter of 9 nm.
- the silica is impregnated with an aqueous solution of zirconium nitrate (impregnation with interaction), filtration, and drying in rotary evaporator, then in an oven at 120 ° C. for 2 hours. The impregnation and drying were repeated a further 2 times so as to obtain a deposit of 0.02% by weight (1.2 g of zirconium per 100 moles of silica).
- the cesium is then also impregnated with an aqueous solution of cesium carbonate, followed by drying, to give a cesium content of about 4% by weight (calculated by weight of metal).
- the catalyst was then calcined at 450 ° C. under air for 3 hours.
- the specific surface of the catalyst thus prepared is 300 m 2 / g.
- Methanol is used from the reaction of a synthesis gas obtained by gasification of black liquor.
- the reaction was carried out in a microreactor at atmospheric pressure, charged with about 3 g of ground catalyst to have particles of about millimeter.
- the catalyst is first dried at 300 ° C. under a flow of 100 ml / min of nitrogen for 30 minutes.
- the catalyst is heated to 300 ° C. and fed with a mixture of methyl propionate, methanol and formalin solution (formalin / methanol / water: 35/15/50 - mass ratios), so that the molar ratios Methanol Methyl propionate and Formol / methyl propionate are 1.45 and 0.187, respectively.
- the temperature of the catalyst is brought to 350 ° C. overnight.
- the yield of methyl methacrylate + methacrylic acid is 9%, with a selectivity of 97%.
- an ethanol-water mixture is used, the ethanol being obtained by fermentation as in Example la.
- the reaction is carried out at a pressure of 30 bar and at a temperature of 900 ° C., with a Ni / Alumina catalyst. On leaving the reactor, the excess water is condensed as well as the heavy impurities.
- the CO / H 2 mixture is cryogenically separated, passing the mixture through a liquid nitrogen trap to retain the CO.
- the condensed gas is then reheated to separate the CO from other impurities (methane, CO 2 , etc.).
- Example 2 For the synthesis of methanol, the synthesis gas of Example 2 is used. The composition of this gas is adjusted to have an H2 / CO / CO2 ratio of 71/23/6 and the CO2 content is 6%. The total pressure of the gas is
- a commercial catalyst Cu-Zn-Al-O, MegaMax 700 is used.
- the reactor is supplied with the gas mixture at 70 bar with a VVH of 1000Oh -1 , and passes over the catalyst at a temperature of 240 ° C.
- the mixture produced gases are then decompressed at atmospheric pressure and the methanol produced is isolated by distillation.
- the selectivity to methanol is 99% and the methanol yield is 95%.
- EXAMPLE 4 Manufacture of formaldehyde by oxidation of methanol The reaction is carried out in a fixed bed reactor. The flow of helium and oxygen is regulated by mass flow meters. The gas flow passes through a methanol-containing evaporator / saturator prepared according to Example 3. The evaporator is either at room temperature or heated by heating ribbons. The temperature of the saturator is adjusted to control the partial pressure of methanol. The temperature of the gas mixture is controlled by a thermocouple at the top of the saturator.
- the gaseous mixture is then sent to the reactor which is placed in an oven.
- the reaction temperature is measured using a thermocouple which is in the catalytic bed.
- the gaseous effluents are analyzed by in-line gas phase chromatography using a microGC equipped with two columns (Molecular sieve and Plot U).
- the catalysts are ground and the 250 micron particle size fraction is mixed with a double amount of silicon carbide of the same particle size and placed in the glass reactors.
- MicrogC calibration was performed with reference gas mixtures, and calibration for condensables (dimethoxymethane, methanol, methyl formate) was performed using the saturator evaporator.
- the catalyst is first activated under a stream of Helium / Oxygen (48 Nml / min - 12 Nml / min) at 340 ° C. for 15 hours and 30 minutes. Then the temperature is brought back to 280 0 C and the accumulation of the product is started.
- Helium / Oxygen 48 Nml / min - 12 Nml / min
- the flow rates of oxygen and helium are respectively 4.7 and 47.6 Nml / min and the concentration of methanol is adjusted to 5% of the reaction medium. (Methanol / O 2 / inert: 5 / 8.5 / 86.5).
- the conversion of methanol is almost complete, and the selectivity to formaldehyde is 90%.
- the products are recovered at the outlet of the reactor in a cold temperature-controlled trap.
- the product obtained is then passed over an anionic resin to remove the acids present, and an aqueous solution of methanol is added to obtain a standard Formol Formalin / Water / Methanol mass ratio formalin: 35/50 / 15.
- the added methanol inhibits the reactions of formalin and thus avoids the subsequent formation of secondary products such as hemi-acetals and polyacetals.
- Example 4 is reproduced but with the following conditions:
- the catalyst is first activated under a stream of Helium / Oxygen (48 Nml / min - 12 Nml / min) at 340 ° C. for 15 hours and 30 minutes. Then, the temperature is reduced to 250 ° C. After stabilization, the products are accumulated. Then the catalyst temperature is increased in trays up to 280 0 C. The flow rates of oxygen and helium are respectively 6.7 and 26.4 Nml / min and the concentration of methanol is adjusted to 37%. (conditions: Methanol / O 2 / inert: 37/13/50) for a VVH of 22000 ml. h "
- the methylal is then separated by distillation from the other products, obtaining its azeotrope with water.
- Example 3 The methanol of Example 3 and the CO of Example 2 are used in conjunction with the ethylene of Example 1-lb to produce 100% renewable methyl propionate under the conditions of Example 1-lc.
- a yield of 18% of methyl propionate relative to methanol is obtained. After obtaining methyl propionate, it is reacted with formaldehyde (obtained as in Example 4) and methanol (obtained as in Example 3) under the conditions of Example 1-2).
- Example 7 Synthesis of Methyl Methacrylate by Reaction of Propionaldehyde and Methylal Example 6 is repeated, but methylal (obtained in Example 5) is used in place of the methanol / formaldehyde mixture, while preserving the molar ratios.
- the yield of methyl methacrylate + methacrylic acid is 6% and the selectivity is 94%.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Wood Science & Technology (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Health & Medical Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Zoology (AREA)
- General Health & Medical Sciences (AREA)
- Biochemistry (AREA)
- Bioinformatics & Cheminformatics (AREA)
- General Engineering & Computer Science (AREA)
- Microbiology (AREA)
- Genetics & Genomics (AREA)
- Biotechnology (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
BRPI0921466A BRPI0921466A2 (pt) | 2008-11-18 | 2009-11-17 | processo para a fabricação de metacrilato de metila derivado de biomassa |
EP09768204A EP2361240A1 (fr) | 2008-11-18 | 2009-11-17 | Procede de fabrication d'un methylacrylate de methyle derive de la biomasse |
CN200980154688.6A CN102282121B (zh) | 2008-11-18 | 2009-11-17 | 制备生物质来源的甲基丙烯酸甲酯的方法 |
US13/129,714 US20110287991A1 (en) | 2008-11-18 | 2009-11-17 | Method for manufacturing a biomass-derived methyl methacrylate |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0857812A FR2938536B1 (fr) | 2008-11-18 | 2008-11-18 | Procede de fabrication d'un methacrylate de methyle derive de la biomasse |
FR0857812 | 2008-11-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2010058119A1 true WO2010058119A1 (fr) | 2010-05-27 |
Family
ID=40786622
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/FR2009/052198 WO2010058119A1 (fr) | 2008-11-18 | 2009-11-17 | Procede de fabrication d'un methylacrylate de methyle derive de la biomasse |
Country Status (6)
Country | Link |
---|---|
US (1) | US20110287991A1 (zh) |
EP (1) | EP2361240A1 (zh) |
CN (1) | CN102282121B (zh) |
BR (1) | BRPI0921466A2 (zh) |
FR (1) | FR2938536B1 (zh) |
WO (1) | WO2010058119A1 (zh) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011077140A2 (en) | 2009-12-21 | 2011-06-30 | Lucite International Uk Limited | Method of producing acrylic and methacrylic acid |
WO2012069813A1 (en) | 2010-11-24 | 2012-05-31 | Lucite International Uk Limited | A process for the production of methacrylic acid and its derivatives and polymers produced therefrom |
WO2012107758A1 (en) | 2011-02-09 | 2012-08-16 | Lucite International Uk Limited | A process for the production of (meth)acrylic acid and derivatives and polymers produced therefrom |
CN104254549A (zh) * | 2012-04-27 | 2014-12-31 | 璐彩特国际英国有限公司 | 用于生产甲基丙烯酸及其衍生物的工艺以及由该工艺生产的聚合物 |
WO2015030580A1 (en) | 2013-08-26 | 2015-03-05 | Stichting Dienst Landbouwkundig Onderzoek | Process for the production of methacrylic acid |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB0403592D0 (en) | 2004-02-18 | 2004-03-24 | Lucite Int Uk Ltd | A catalyst system |
US9382491B2 (en) | 2012-07-03 | 2016-07-05 | Sartec Corporation | Hydrocarbon synthesis methods, apparatus, and systems |
WO2014008355A1 (en) | 2012-07-03 | 2014-01-09 | Mcneff Clayton V | Hydrocarbon synthesis methods, apparatus, and systems |
CN102962062B (zh) * | 2012-12-11 | 2014-09-17 | 西南化工研究设计院有限公司 | 一种由甲醛与丙酸甲酯合成甲基丙烯酸甲酯的催化剂及其制备方法 |
CN104725225B (zh) * | 2013-12-23 | 2017-01-18 | 中国科学院大连化学物理研究所 | 制备聚甲氧基二甲醚羰化物及甲氧基乙酸甲酯的方法 |
CN107428879A (zh) * | 2015-04-16 | 2017-12-01 | 安耐罗技术股份有限公司 | 生物质衍生的化学中间体 |
US10308584B2 (en) | 2016-02-25 | 2019-06-04 | 3M Innovative Properties Company | Methods of making (alk)acrylic esters in flow reactors |
US10239812B2 (en) | 2017-04-27 | 2019-03-26 | Sartec Corporation | Systems and methods for synthesis of phenolics and ketones |
CN107337600A (zh) * | 2017-07-04 | 2017-11-10 | 湖北三里枫香科技有限公司 | 一种甲醇和醋酸甲酯生产甲基丙烯酸甲酯的方法及工艺装置 |
US10544381B2 (en) | 2018-02-07 | 2020-01-28 | Sartec Corporation | Methods and apparatus for producing alkyl esters from a reaction mixture containing acidified soap stock, alcohol feedstock, and acid |
US10696923B2 (en) | 2018-02-07 | 2020-06-30 | Sartec Corporation | Methods and apparatus for producing alkyl esters from lipid feed stocks, alcohol feedstocks, and acids |
MX2023003071A (es) * | 2020-09-25 | 2023-05-24 | Carbon Tech Holdings Llc | Biorreducción de minerales metálicos integrados con pirólisis de biomasa. |
CN112851505B (zh) * | 2021-01-08 | 2022-04-26 | 西南化工研究设计院有限公司 | 一种丙烯酸甲酯连续气相加氢制丙酸甲酯工艺 |
CN112851507A (zh) * | 2021-01-25 | 2021-05-28 | 西南化工研究设计院有限公司 | 一种乙醇合成甲基丙烯酸甲酯的工艺 |
US20230020752A1 (en) | 2021-07-09 | 2023-01-19 | Carbon Technology Holdings, LLC | Producing biocarbon pellets with high fixed-carbon content and optimized reactivity, and biocarbon pellets obtained therefrom |
Citations (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3701798A (en) | 1965-12-03 | 1972-10-31 | Eastman Kodak Co | Synthesis of unsaturated compounds |
FR2223080A1 (zh) | 1972-10-06 | 1974-10-25 | Rohm & Haas | |
FR2347330A1 (fr) | 1976-04-10 | 1977-11-04 | Basf Ag | Procede de preparation d'acide methacrylique et de methacrylate de methyle |
GB1491183A (en) | 1976-04-06 | 1977-11-09 | Roehm Gmbh | Preparation of methacrylic acid esters and nitrile |
FR2377995A1 (fr) | 1977-01-20 | 1978-08-18 | Roehm Gmbh | Procede de preparation de l'acide methacrylique, de son nitrile et de ses esters par reaction respectivement de l'acide propionique, de son nitrile et des esters avec le metrylal |
GB2001647A (en) * | 1977-07-25 | 1979-02-07 | Roehm Gmbh | Process for the preparation of methacrylic acid and the esters and nitrile thereof |
EP0286981A2 (de) * | 1987-04-15 | 1988-10-19 | Hoechst Aktiengesellschaft | Verfahren zur Herstellung von Carbonsäuremethylestern |
EP0666831A1 (en) | 1992-11-02 | 1995-08-16 | Kvaerner Pulping Ab | Process associated with the gasification of cellulose spent liquors |
US20050059839A1 (en) * | 2003-09-15 | 2005-03-17 | The Regents Of The University Of California | Process and catalysts for the oxidation of methanol and/or ethanol |
WO2005095320A1 (en) * | 2004-04-02 | 2005-10-13 | Ciba Specialty Chemicals Water Treatments Limited | Preparation of acrylic acid derivatives from alpha or beta-hydroxy carboxylic acids |
WO2006114506A1 (fr) * | 2005-04-25 | 2006-11-02 | Arkema France | Procede de preparation d’acide acrylique a partir de glycerol |
US7294225B2 (en) | 2000-11-15 | 2007-11-13 | Chemrec Aktiebolag | Process for production of synthesis gas in combination with the maintenance of the energy balance for a pulp mill |
WO2008067627A2 (en) * | 2006-12-05 | 2008-06-12 | Braskem S.A. | A method for the production of one or more olefins, an olefin, and a polymer |
-
2008
- 2008-11-18 FR FR0857812A patent/FR2938536B1/fr not_active Expired - Fee Related
-
2009
- 2009-11-17 BR BRPI0921466A patent/BRPI0921466A2/pt not_active Application Discontinuation
- 2009-11-17 EP EP09768204A patent/EP2361240A1/fr not_active Withdrawn
- 2009-11-17 CN CN200980154688.6A patent/CN102282121B/zh active Active
- 2009-11-17 US US13/129,714 patent/US20110287991A1/en not_active Abandoned
- 2009-11-17 WO PCT/FR2009/052198 patent/WO2010058119A1/fr active Application Filing
Patent Citations (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3701798A (en) | 1965-12-03 | 1972-10-31 | Eastman Kodak Co | Synthesis of unsaturated compounds |
FR2223080A1 (zh) | 1972-10-06 | 1974-10-25 | Rohm & Haas | |
GB1491183A (en) | 1976-04-06 | 1977-11-09 | Roehm Gmbh | Preparation of methacrylic acid esters and nitrile |
FR2347330A1 (fr) | 1976-04-10 | 1977-11-04 | Basf Ag | Procede de preparation d'acide methacrylique et de methacrylate de methyle |
FR2377995A1 (fr) | 1977-01-20 | 1978-08-18 | Roehm Gmbh | Procede de preparation de l'acide methacrylique, de son nitrile et de ses esters par reaction respectivement de l'acide propionique, de son nitrile et des esters avec le metrylal |
FR2400499A2 (fr) | 1977-07-25 | 1979-03-16 | Roehm Gmbh | Procede de preparation de l'acide methacrylique, de ses esters et de son nitrile |
GB2001647A (en) * | 1977-07-25 | 1979-02-07 | Roehm Gmbh | Process for the preparation of methacrylic acid and the esters and nitrile thereof |
EP0286981A2 (de) * | 1987-04-15 | 1988-10-19 | Hoechst Aktiengesellschaft | Verfahren zur Herstellung von Carbonsäuremethylestern |
EP0666831A1 (en) | 1992-11-02 | 1995-08-16 | Kvaerner Pulping Ab | Process associated with the gasification of cellulose spent liquors |
US7294225B2 (en) | 2000-11-15 | 2007-11-13 | Chemrec Aktiebolag | Process for production of synthesis gas in combination with the maintenance of the energy balance for a pulp mill |
US20050059839A1 (en) * | 2003-09-15 | 2005-03-17 | The Regents Of The University Of California | Process and catalysts for the oxidation of methanol and/or ethanol |
WO2005095320A1 (en) * | 2004-04-02 | 2005-10-13 | Ciba Specialty Chemicals Water Treatments Limited | Preparation of acrylic acid derivatives from alpha or beta-hydroxy carboxylic acids |
WO2006114506A1 (fr) * | 2005-04-25 | 2006-11-02 | Arkema France | Procede de preparation d’acide acrylique a partir de glycerol |
WO2008067627A2 (en) * | 2006-12-05 | 2008-06-12 | Braskem S.A. | A method for the production of one or more olefins, an olefin, and a polymer |
Non-Patent Citations (3)
Title |
---|
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, vol. 36, no. 11, 1997, pages 4600 - 4608 |
SPIVEY AND CO, INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, vol. 36, 1997, pages 4600 - 4608, XP002534268 * |
XIUMIN MA AND CO, CATALYSIS COMMUNICATIONS, vol. 9, 23 May 2007 (2007-05-23), pages 70 - 74, XP002534269 * |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2011077140A2 (en) | 2009-12-21 | 2011-06-30 | Lucite International Uk Limited | Method of producing acrylic and methacrylic acid |
US8933179B2 (en) | 2009-12-21 | 2015-01-13 | Lucite International Uk Limited | Method of producing arcylic and methacrylic acid |
WO2012069813A1 (en) | 2010-11-24 | 2012-05-31 | Lucite International Uk Limited | A process for the production of methacrylic acid and its derivatives and polymers produced therefrom |
US9174913B2 (en) | 2010-11-24 | 2015-11-03 | Lucite International Uk Limited | Process for the production of methacrylic acid and its derivatives and polymers produced therefrom |
WO2012107758A1 (en) | 2011-02-09 | 2012-08-16 | Lucite International Uk Limited | A process for the production of (meth)acrylic acid and derivatives and polymers produced therefrom |
US9216938B2 (en) | 2011-02-09 | 2015-12-22 | Lucite International Uk Limited | Process for the production of (meth)acrylic acid and derivatives and polyers produced therefrom |
US9890103B2 (en) | 2011-02-09 | 2018-02-13 | Lucite International Uk Limited | Process for the production of (meth)acrylic acid and derivatives and polymers produced therefrom |
CN104254549A (zh) * | 2012-04-27 | 2014-12-31 | 璐彩特国际英国有限公司 | 用于生产甲基丙烯酸及其衍生物的工艺以及由该工艺生产的聚合物 |
WO2015030580A1 (en) | 2013-08-26 | 2015-03-05 | Stichting Dienst Landbouwkundig Onderzoek | Process for the production of methacrylic acid |
Also Published As
Publication number | Publication date |
---|---|
FR2938536B1 (fr) | 2012-07-13 |
CN102282121B (zh) | 2016-08-24 |
US20110287991A1 (en) | 2011-11-24 |
EP2361240A1 (fr) | 2011-08-31 |
CN102282121A (zh) | 2011-12-14 |
BRPI0921466A2 (pt) | 2016-01-12 |
FR2938536A1 (fr) | 2010-05-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2010058119A1 (fr) | Procede de fabrication d'un methylacrylate de methyle derive de la biomasse | |
WO2010079293A1 (fr) | Procede de fabrication d'un methacrylate de methyle derive de la biomasse | |
KR101649997B1 (ko) | 에틸렌-부틸렌 공중합체의 제조를 위한 통합 방법, 에틸렌-부틸렌 공중합체 및 재생성 천연 원자재로부터 유래한 공단량체로서의 에틸렌 및 1-부틸렌의 용도 | |
EP2361239B1 (fr) | Procédé de fabrication de méthylmercaptopropionaldehyde et de methionine à partir de matières premières renouvelables | |
FR2934264A1 (fr) | Fabrication d'esters de vinyle a partir de matieres renouvelables, esters de vinyle obtenus et utilisations | |
FR2931822A1 (fr) | Methacrylate de methyle derive de la biomasse, procede de fabrication, utilisations et polymeres correspondants. | |
EP2321253A2 (fr) | Procede de synthese d'esters de l'acide acrylique bioressources | |
EP2774969B1 (en) | Process for converting bio-oil | |
FR2997397A1 (fr) | Procede de synthese directe d'aldehydes insatures a partir de melanges d'alcools | |
CA2931704A1 (fr) | Procede de deshydratation d'un melange contenant de l'ethanol et de l'isopropanol | |
WO2010007327A2 (fr) | Fabrication d'anhydride maleique a partir de matieres renouvelables, anhydride maleique obtenu et utilisations | |
FR2957594A1 (fr) | Procede de fabrication d'acide acrylique bio-ressource de grade polymere a partir de glycerol | |
FR2932804A1 (fr) | Polymere d'acroleine derive de matiere premiere renouvelable, son procede d'obtention et ses utilisations | |
JP2017066149A (ja) | バイオマス由来のメチルメタクリレートの製造方法 | |
EP4003949A1 (fr) | Procede de traitement d'une composition comprenant de la vanilline naturelle | |
EP2718452A1 (fr) | Procede de synthese de composes hydrocarbones bi-fonctionnels a partir de biomasse | |
EP3126318A1 (fr) | Procédé de synthèse directe de (méth)acroléine a partir d'éthers et/ou acétals | |
BRPI0805612A2 (pt) | processo de produção de uma mistura de n-butenos adequada para a produção de propeno por reação de metátese com eteno, e, mistura de n-butenos |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
WWE | Wipo information: entry into national phase |
Ref document number: 200980154688.6 Country of ref document: CN |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 09768204 Country of ref document: EP Kind code of ref document: A1 |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2009768204 Country of ref document: EP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 13129714 Country of ref document: US |
|
ENP | Entry into the national phase |
Ref document number: PI0921466 Country of ref document: BR Kind code of ref document: A2 Effective date: 20110518 |