CN1277607C - Solid acid catalyst for hydration of epoxy ethane to produce ethandiol - Google Patents
Solid acid catalyst for hydration of epoxy ethane to produce ethandiol Download PDFInfo
- Publication number
- CN1277607C CN1277607C CN 200310108696 CN200310108696A CN1277607C CN 1277607 C CN1277607 C CN 1277607C CN 200310108696 CN200310108696 CN 200310108696 CN 200310108696 A CN200310108696 A CN 200310108696A CN 1277607 C CN1277607 C CN 1277607C
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- China
- Prior art keywords
- catalyst
- acid catalyst
- solid acid
- ethylene glycol
- hours
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- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 title claims abstract description 164
- 239000003054 catalyst Substances 0.000 title claims abstract description 109
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 title claims abstract description 47
- 238000006703 hydration reaction Methods 0.000 title claims abstract description 35
- 230000036571 hydration Effects 0.000 title claims abstract description 27
- 239000011973 solid acid Substances 0.000 title claims abstract description 22
- 239000010955 niobium Substances 0.000 claims abstract description 18
- 238000004519 manufacturing process Methods 0.000 claims abstract description 17
- 229910052758 niobium Inorganic materials 0.000 claims abstract description 17
- GUCVJGMIXFAOAE-UHFFFAOYSA-N niobium atom Chemical compound [Nb] GUCVJGMIXFAOAE-UHFFFAOYSA-N 0.000 claims abstract 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 27
- 239000000203 mixture Substances 0.000 claims description 22
- 229910000765 intermetallic Inorganic materials 0.000 claims description 13
- 229910052684 Cerium Inorganic materials 0.000 claims description 11
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 10
- ZSLUVFAKFWKJRC-IGMARMGPSA-N 232Th Chemical compound [232Th] ZSLUVFAKFWKJRC-IGMARMGPSA-N 0.000 claims description 7
- 229910052776 Thorium Inorganic materials 0.000 claims description 7
- 239000011230 binding agent Substances 0.000 claims description 7
- ZMIGMASIKSOYAM-UHFFFAOYSA-N cerium Chemical compound [Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce][Ce] ZMIGMASIKSOYAM-UHFFFAOYSA-N 0.000 claims description 7
- 229910052804 chromium Inorganic materials 0.000 claims description 6
- 239000011651 chromium Substances 0.000 claims description 6
- 239000002808 molecular sieve Substances 0.000 claims description 6
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052751 metal Inorganic materials 0.000 claims description 5
- 239000002184 metal Substances 0.000 claims description 5
- 239000000377 silicon dioxide Substances 0.000 claims description 5
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims description 4
- 239000000470 constituent Substances 0.000 claims description 4
- 229910044991 metal oxide Inorganic materials 0.000 claims description 4
- 150000004706 metal oxides Chemical class 0.000 claims description 4
- 229910052750 molybdenum Inorganic materials 0.000 claims description 4
- 239000011733 molybdenum Substances 0.000 claims description 4
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims description 4
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical group [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 3
- 229910052721 tungsten Inorganic materials 0.000 claims description 3
- 239000010937 tungsten Substances 0.000 claims description 3
- 241000269350 Anura Species 0.000 claims description 2
- 238000006243 chemical reaction Methods 0.000 abstract description 64
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 38
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 abstract description 17
- 239000007788 liquid Substances 0.000 abstract description 11
- 230000000694 effects Effects 0.000 abstract description 9
- 238000005265 energy consumption Methods 0.000 abstract description 7
- 230000000887 hydrating effect Effects 0.000 abstract description 4
- 239000003377 acid catalyst Substances 0.000 abstract description 3
- 150000002736 metal compounds Chemical class 0.000 abstract description 3
- 230000007797 corrosion Effects 0.000 abstract description 2
- 238000005260 corrosion Methods 0.000 abstract description 2
- 238000009776 industrial production Methods 0.000 abstract description 2
- 230000003197 catalytic effect Effects 0.000 abstract 2
- 239000012752 auxiliary agent Substances 0.000 abstract 1
- 230000007547 defect Effects 0.000 abstract 1
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 229910052715 tantalum Inorganic materials 0.000 abstract 1
- GUVRBAGPIYLISA-UHFFFAOYSA-N tantalum atom Chemical compound [Ta] GUVRBAGPIYLISA-UHFFFAOYSA-N 0.000 abstract 1
- 229910052720 vanadium Inorganic materials 0.000 abstract 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 abstract 1
- 238000000034 method Methods 0.000 description 33
- 239000000243 solution Substances 0.000 description 20
- 239000002253 acid Substances 0.000 description 18
- 238000001035 drying Methods 0.000 description 13
- 238000000465 moulding Methods 0.000 description 12
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 10
- 239000013590 bulk material Substances 0.000 description 10
- 229910017604 nitric acid Inorganic materials 0.000 description 10
- 238000002360 preparation method Methods 0.000 description 10
- 238000001291 vacuum drying Methods 0.000 description 10
- 206010013786 Dry skin Diseases 0.000 description 9
- 238000004898 kneading Methods 0.000 description 9
- 239000007787 solid Substances 0.000 description 9
- 230000008569 process Effects 0.000 description 8
- 238000012360 testing method Methods 0.000 description 8
- 239000007864 aqueous solution Substances 0.000 description 7
- 239000012018 catalyst precursor Substances 0.000 description 7
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 6
- 230000001590 oxidative effect Effects 0.000 description 6
- 239000000843 powder Substances 0.000 description 6
- PHFQLYPOURZARY-UHFFFAOYSA-N chromium trinitrate Chemical compound [Cr+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PHFQLYPOURZARY-UHFFFAOYSA-N 0.000 description 5
- 230000008030 elimination Effects 0.000 description 5
- 238000003379 elimination reaction Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 5
- 238000002803 maceration Methods 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- XNHGKSMNCCTMFO-UHFFFAOYSA-D niobium(5+);oxalate Chemical compound [Nb+5].[Nb+5].[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O.[O-]C(=O)C([O-])=O XNHGKSMNCCTMFO-UHFFFAOYSA-D 0.000 description 5
- 229910001220 stainless steel Inorganic materials 0.000 description 5
- 239000010935 stainless steel Substances 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 229910004298 SiO 2 Inorganic materials 0.000 description 4
- -1 alkane ammonium salt Chemical class 0.000 description 4
- 238000006555 catalytic reaction Methods 0.000 description 4
- HSJPMRKMPBAUAU-UHFFFAOYSA-N cerium(3+);trinitrate Chemical compound [Ce+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O HSJPMRKMPBAUAU-UHFFFAOYSA-N 0.000 description 4
- 238000010335 hydrothermal treatment Methods 0.000 description 4
- 150000002822 niobium compounds Chemical class 0.000 description 4
- 238000005303 weighing Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- KMTRUDSVKNLOMY-UHFFFAOYSA-N Ethylene carbonate Chemical compound O=C1OCCO1 KMTRUDSVKNLOMY-UHFFFAOYSA-N 0.000 description 3
- MUBZPKHOEPUJKR-UHFFFAOYSA-N Oxalic acid Chemical compound OC(=O)C(O)=O MUBZPKHOEPUJKR-UHFFFAOYSA-N 0.000 description 3
- APUPEJJSWDHEBO-UHFFFAOYSA-P ammonium molybdate Chemical compound [NH4+].[NH4+].[O-][Mo]([O-])(=O)=O APUPEJJSWDHEBO-UHFFFAOYSA-P 0.000 description 3
- 229940010552 ammonium molybdate Drugs 0.000 description 3
- 235000018660 ammonium molybdate Nutrition 0.000 description 3
- 239000011609 ammonium molybdate Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- KRKNYBCHXYNGOX-UHFFFAOYSA-N citric acid Chemical compound OC(=O)CC(O)(C(O)=O)CC(O)=O KRKNYBCHXYNGOX-UHFFFAOYSA-N 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 3
- 239000000945 filler Substances 0.000 description 3
- 238000004817 gas chromatography Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000004445 quantitative analysis Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- TXUICONDJPYNPY-UHFFFAOYSA-N (1,10,13-trimethyl-3-oxo-4,5,6,7,8,9,11,12,14,15,16,17-dodecahydrocyclopenta[a]phenanthren-17-yl) heptanoate Chemical compound C1CC2CC(=O)C=C(C)C2(C)C2C1C1CCC(OC(=O)CCCCCC)C1(C)CC2 TXUICONDJPYNPY-UHFFFAOYSA-N 0.000 description 2
- JECYNCQXXKQDJN-UHFFFAOYSA-N 2-(2-methylhexan-2-yloxymethyl)oxirane Chemical compound CCCCC(C)(C)OCC1CO1 JECYNCQXXKQDJN-UHFFFAOYSA-N 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 2
- 229910021626 Tin(II) chloride Inorganic materials 0.000 description 2
- 238000007171 acid catalysis Methods 0.000 description 2
- 150000007513 acids Chemical class 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 239000003426 co-catalyst Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000005530 etching Methods 0.000 description 2
- 238000011156 evaluation Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 229910052732 germanium Inorganic materials 0.000 description 2
- GNPVGFCGXDBREM-UHFFFAOYSA-N germanium atom Chemical compound [Ge] GNPVGFCGXDBREM-UHFFFAOYSA-N 0.000 description 2
- YBMRDBCBODYGJE-UHFFFAOYSA-N germanium dioxide Chemical compound O=[Ge]=O YBMRDBCBODYGJE-UHFFFAOYSA-N 0.000 description 2
- 239000011964 heteropoly acid Substances 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 238000005470 impregnation Methods 0.000 description 2
- JVTAAEKCZFNVCJ-UHFFFAOYSA-N lactic acid Chemical compound CC(O)C(O)=O JVTAAEKCZFNVCJ-UHFFFAOYSA-N 0.000 description 2
- 150000007522 mineralic acids Chemical class 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 229940068984 polyvinyl alcohol Drugs 0.000 description 2
- 235000019422 polyvinyl alcohol Nutrition 0.000 description 2
- 238000012805 post-processing Methods 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 238000011160 research Methods 0.000 description 2
- 238000009938 salting Methods 0.000 description 2
- 238000013112 stability test Methods 0.000 description 2
- 239000001119 stannous chloride Substances 0.000 description 2
- 235000011150 stannous chloride Nutrition 0.000 description 2
- VGBPIHVLVSGJGR-UHFFFAOYSA-N thorium(4+);tetranitrate Chemical compound [Th+4].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VGBPIHVLVSGJGR-UHFFFAOYSA-N 0.000 description 2
- BJEPYKJPYRNKOW-REOHCLBHSA-N (S)-malic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O BJEPYKJPYRNKOW-REOHCLBHSA-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
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 229920002799 BoPET Polymers 0.000 description 1
- 229920000858 Cyclodextrin Polymers 0.000 description 1
- 229920001353 Dextrin Polymers 0.000 description 1
- 239000004375 Dextrin Substances 0.000 description 1
- FEWJPZIEWOKRBE-JCYAYHJZSA-N Dextrotartaric acid Chemical compound OC(=O)[C@H](O)[C@@H](O)C(O)=O FEWJPZIEWOKRBE-JCYAYHJZSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 1
- 239000005041 Mylar™ Substances 0.000 description 1
- IYEACMDEYLNJEE-UHFFFAOYSA-N N.[Nb+5] Chemical compound N.[Nb+5] IYEACMDEYLNJEE-UHFFFAOYSA-N 0.000 description 1
- FEWJPZIEWOKRBE-UHFFFAOYSA-N Tartaric acid Natural products [H+].[H+].[O-]C(=O)C(O)C(O)C([O-])=O FEWJPZIEWOKRBE-UHFFFAOYSA-N 0.000 description 1
- 235000011054 acetic acid Nutrition 0.000 description 1
- QANURPDUWUFOMP-UHFFFAOYSA-N acetic acid;niobium Chemical compound [Nb].CC(O)=O QANURPDUWUFOMP-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 239000003570 air Substances 0.000 description 1
- 125000001931 aliphatic group Chemical group 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 229920000180 alkyd Polymers 0.000 description 1
- BJEPYKJPYRNKOW-UHFFFAOYSA-N alpha-hydroxysuccinic acid Natural products OC(=O)C(O)CC(O)=O BJEPYKJPYRNKOW-UHFFFAOYSA-N 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 239000003957 anion exchange resin Substances 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000003990 capacitor Substances 0.000 description 1
- 229920003064 carboxyethyl cellulose Polymers 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000001413 cellular effect Effects 0.000 description 1
- 235000015165 citric acid Nutrition 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000002079 cooperative effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000002950 deficient Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 235000019425 dextrin Nutrition 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 229920001249 ethyl cellulose Polymers 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 235000011087 fumaric acid Nutrition 0.000 description 1
- 229940119177 germanium dioxide Drugs 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 239000004310 lactic acid Substances 0.000 description 1
- 235000014655 lactic acid Nutrition 0.000 description 1
- HCWCAKKEBCNQJP-UHFFFAOYSA-N magnesium orthosilicate Chemical compound [Mg+2].[Mg+2].[O-][Si]([O-])([O-])[O-] HCWCAKKEBCNQJP-UHFFFAOYSA-N 0.000 description 1
- 239000000391 magnesium silicate Substances 0.000 description 1
- 229910052919 magnesium silicate Inorganic materials 0.000 description 1
- 235000019792 magnesium silicate Nutrition 0.000 description 1
- 239000001630 malic acid Substances 0.000 description 1
- 235000011090 malic acid Nutrition 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000001404 mediated effect Effects 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000006408 oxalic acid Nutrition 0.000 description 1
- 150000002924 oxiranes Chemical group 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229910052573 porcelain Inorganic materials 0.000 description 1
- 125000001453 quaternary ammonium group Chemical group 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 230000036632 reaction speed Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- HFHDHCJBZVLPGP-UHFFFAOYSA-N schardinger α-dextrin Chemical compound O1C(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC(C(O)C2O)C(CO)OC2OC(C(C2O)O)C(CO)OC2OC2C(O)C(O)C1OC2CO HFHDHCJBZVLPGP-UHFFFAOYSA-N 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 239000008247 solid mixture Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000011975 tartaric acid Substances 0.000 description 1
- 235000002906 tartaric acid Nutrition 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The present invention relates to a solid acid catalyst for producing glycol by hydrating epoxy ethane, which mainly solves the defects of high water ratio, large energy consumption and high production cost of the existing epoxy ethane non-catalytic hydration reaction or equipment corrosion, environmental pollution of a liquid acid catalyst for catalytic hydration and poor stability of a solid acid catalyst, or the stability and the activity of the solid acid catalyst can not simultaneously exist. The present invention provides a solid acid catalyst for producing glycol by hydrating epoxy ethane and has the technical scheme that oxide loaded with niobium on a carrier of the oxide is used as a main active component; at least one auxiliary agent selected from IVA and IVB metal compounds and metal compounds of vanadium or tantalum non-forcefully added. The prepared catalyst is used for a reaction for producing glycol by hydrating epoxy ethane, has good activity and selectivity, and is suitable for low water ratio operation. Meanwhile, the catalyst has good stability. The energy consumption is obviously reduced, and the production cost is greatly reduced. The present invention can be used in industrial production of glycol.
Description
Technical field
The present invention relates to a kind of solid acid catalyst that ethylene glycol is produced in the ethylene oxide hydration reaction that is used for, particularly about being used for a kind of Niobic Acid agent that ethylene glycol is produced in the ethylene oxide hydration reaction.
Background technology
Ethylene glycol is important aliphatic dihydroxy alcohol, and is of many uses, and main application is to produce mylar, comprises fiber, film and engineering plastics.Also can directly be used as cooling agent and antifreezing agent, also be simultaneously to produce the indispensable materials of product such as alkyd resins, plasticizer, paint, adhesive, surfactant, explosive and capacitor electrolyte.
With oxirane is feedstock production ethylene glycol, mainly contain two kinds of process routes: a kind of is direct hydration method, oxirane and water react generation ethylene glycol under certain condition, and reaction does not need catalyst just can carry out, and is divided into two kinds of technologies of catalysis hydration and on-catalytic hydration; Another kind is the ethylene carbonate method, promptly oxirane under catalyst action, elder generation and CO
2Reaction generates ethylene carbonate, and hydrolysis generates ethylene glycol then.
Industrial production ethylene glycol adopts the uncatalysed processes of hydration method at present, also is current method of producing unique use.This method is not used catalyst, the mol ratio of water and oxirane (hereinafter to be referred as water than) be 20～25: 1,150～200 ℃ of reaction temperatures, reaction pressure 0.8～2.0MPa, oxirane conversion ratio be near 100%, glycol selectivity 88～90%.This method disadvantage is that energy consumption is big, the evaporation and concentration long flow path, for example in refined product ethylene glycol step, when the feed water ratio is 20, evaporate and remove the no water that is approximately 19 times of ethylene glycol, need to consume and count 170 kilocalories heat energy, mean that producing 1 ton of ethylene glycol need consume about 5.5 tons of steam with every mole of ethylene glycol, make that this method equipment investment is big, the production cost height.Simultaneously in the presence of catalyst-free, hydration reaction speed is slow, the industrial need adopted bigger pipeline reactor, caused the increase of transmission and mass transfer energy, in addition, a high proportion of feed water is than the glycol product selectivity is improved significantly, and consumptions such as the accessory substance diethylene glycol that generates, triethylene glycol are little, and the ethylene glycol demand growth is very fast, thereby, develop a kind of preparing ethandiol by catalyzing epoxyethane hydration technology, improve this technology whole synthesis performance and seem particularly important.
Catalysis hydration is produced the method for ethylene glycol the earliest, once adopts inorganic acid as catalyst, makes catalyst as using sulfuric acid, and oxirane can all transform, and the ethylene glycol yield is 88～90%.But because liquid acid catalyst etching apparatus, contaminated environment, there are problems in product quality, need add alkali neutralization and separation circuit during post processing, and product selectivity is compared with the on-catalytic hydration and be there is no clear superiority and can say, therefore, traditional acid catalysis hydrating process is eliminated, and does not re-use.
For overcoming the shortcoming of inorganic acid catalysis hydration, people have carried out many-sided improvement research to the catalyst that is used for hydration of epoxy ethane to prepare ethandiol, and the research focus mainly adopts solid acid as catalyst such as ion exchange resin, heteropoly acid.
US 5874653 discloses a kind of anion exchange resin of quaternary ammonium group that has as the ethylene oxide hydration catalyst.At 80～200 ℃ of reaction temperatures, reaction pressure 200～3000KPa, water is than 1～15: react under 1 the condition, the conversion ratio of oxirane is near 100%, the selectivity 95% of ethylene glycol.But the remarkable shortcoming of this catalyst system and catalyzing is that the resin catalyst heat resistance is poor, and in the hydration reaction temperature range, the expansion situation of catalyst is more serious, and it is very fast to cause the reactor bed pressure drop to be risen, and shortens catalyst service life.
JP82106631 discloses a kind of K
2MoO
4-KI catalyst makes oxirane and carbon dioxide generate ethylene carbonate 160 ℃ of reactions, is catalyst then with the aluminium oxide, 140 ℃ of reaction temperatures, under the pressure 2.25MPa condition, hydrolysis obtains the ethylene glycol product, oxirane conversion ratio 100%, glycol selectivity 99.8%.Use the distinguishing feature of above-mentioned heteropolyacid salt catalyst to be: when catalyst was dissolvable in water water, oxirane conversion ratio and product selectivity were higher, but catalyst easily runs off, and poor stability has brought unnecessary trouble to postprocessing working procedures; When catalyst was water insoluble, the oxirane conversion ratio obviously reduced, and the selectivity of ethylene glycol is relatively poor.
US5874653 discloses a kind of method for preparing ethylene glycol, use the agent of poly-organosilicon alkane ammonium salt in catalysis, oxirane and water prepared in reaction ethylene glycol, the disclosed embodiment reaction result of document is: reaction was carried out 600 hours, catalyst has good selectivity and stability, selectivity is 93～95%, but the oxirane conversion ratio is on the low side, and the highest have only 57.9%.
Japanese patent laid-open 06-179633 discloses a kind of manufacture method of aryl ethylene glycol, this patent is that the aryl rings oxidative ethane is handled with niobic acid in water and aqueous solvent, can effectively the epoxide ring in the aryl rings oxidative ethane partly be added water decomposition, the yield of aryl ethylene glycol is higher, the shortcoming of this method is that water is than too high, separation brings huge energy consumption to ethylene glycol in the existence of big water gaging, causes production cost higher; And document does not relate to the stability of catalyst.
Japanese patent laid-open 7-53219 has introduced a kind of columbic acid particle and preparation method thereof, and this columbic acid particle contains acidity H
0: the acid amount A below-3.0 is 0.35 mM/more than the gram, wherein be H more than 50%
0: the strong acid amount below-5.6, the document do not relate to and are used for the reaction that hydration prepares ethylene glycol, show according to the study, and the columbic acid particle of preparation is not suitable for the catalyzing epoxyethane hydration reaction for preparing glycol because acidity is strong excessively.
Summary of the invention
Technical problem to be solved by this invention is to overcome in the past in the document, oxirane on-catalytic hydration reaction water is than higher, energy consumption is big, the cost height, or the liquid acid catalyst etching apparatus of catalysis hydration use, contaminated environment, solid acid catalyst poor stability or stability and the active defective that can not take into account simultaneously, a kind of solid acid catalyst that ethylene oxide hydration is produced ethylene glycol that is used for is provided, this catalyst is used for ethylene oxide hydration prepared in reaction ethylene glycol, not only has good activity, selectivity is suitable for low water than operation, and has good stable simultaneously, can significantly reduce energy energy consumption, reduce production costs significantly.
For solving the problems of the technologies described above, the technical solution used in the present invention is as follows: a kind of solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol, to be selected from a kind of or its mixture in aluminium oxide, silica or the molecular sieve as carrier, the following active constituent of load on carrier, the percentage that accounts for vehicle weight is:
A) metal oxide of 5～20% niobiums;
B) 0.01～20% be selected from the metallic compound of IVA at least a;
C) 0.001～10% be selected from the metallic compound of VIB at least a;
D) 0～5% be selected from the metallic compound of cerium or thorium at least a.
In the technique scheme, in vehicle weight percentage, the metal oxide consumption of niobium is preferred 5～10%, and it is preferred 0.05～15% to be selected from the metallic compound consumption of IVA, is selected from the metallic compound consumption preferred 0.05～10% of VIB; Also contain the metallic compound that is selected from cerium or thorium in the catalyst component, its consumption is by vehicle weight percentage preferred 0.001～3%.Be selected from the metallic compound consumption preferred 0.001～3% of cerium or thorium.
In the technique scheme, described oxide carrier can use separately, also can mix with certain proportion and use, the preferred Alpha-alumina of wherein said aluminium oxide, the preferred SAPO series of described molecular sieve molecular sieve.
Catalyst of the present invention also contains counts 1～10% binding agent with vehicle weight percentage, the binding agent that often uses as catalyst field such as inorganic clay, methyl or ethyl or carboxyethyl cellulose, magnesium silicate fiber element, polyvinyl alcohol, dextrin, rare nitric acid or water.
Catalyst of the present invention can use method for preparing catalyst commonly used such as mixing method, infusion process or coprecipitation to make.This specification is that example describes the Preparation of catalysts method with the blending method, but is not limited to this method.Blending method is that carrier, active constituent niobium source and co-catalyst are mixed, and the moulding of catalyst for the benefit of improves catalyst strength, can add an amount of binding agent in the mixed process, fully mediate then, make shaping of catalyst after, be prepared from through steps such as super-dry, roastings.Concrete preparation process is as follows:
1, niobium source:
Solid state powder form with commercially available niobic acid, niobium oxalate, acetic acid niobium or niobium ammino-complex is introduced, and perhaps introduces with niobium compound solution form, and niobium compound solution is prepared as follows:
Take by weighing a certain amount of niobium compound, be generally commercially available niobic acid (Nb
2O
5NH
2O, n is 1-5), be dissolved in the acid solution, acid solution can be organic acid solns such as oxalic acid, acetic acid, tartaric acid, citric acid, malic acid, lactic acid, fumaric acid, the concentration of niobium compound in the acid solution is as long as below saturated concentration, no particular determination is generally 0.5～30% (weight), is preferably 1～20% (weight);
2, IVA metal (germanium, tin, lead) source:
Introduce with oxide, nitrate, chloride or acetate solid state powder form, or be dissolved in the rare nitric acid or dilute hydrochloric acid solution of 5～15% (weight), be mixed with salting liquid; In fact, as long as it can be mixed with the aqueous solution, there is no particular restriction on the method.
3, vib metal (chromium, molybdenum, tungsten), cerium or thorium source:
Introduce with oxide, nitrate, chloride, ammonium salt or acetate solid state powder form, or take by weighing the catalyst formulation requirement, be mixed with certain density salting liquid according to conventional method.
4, Preparation of Catalyst
With above-mentioned niobium source, after IVA metal (germanium, tin, lead) source, vib metal (chromium, molybdenum, tungsten), cerium or thorium source, carrier unit's powder and binding agent are fully mediated in kneader, make certain shape, catalyst shape can be made different shapes such as cylindric, spherical, disk, tubular, cellular or Raschig ring with conventional method.℃ carry out drying in room temperature～200, preferred 100～200 ℃, 1～5 hour drying time, preferred 1～3 hour, can adopt vacuum drying or aeration-drying when dry; Carry out roasting then, 100～1000 ℃ of sintering temperatures, preferred 200～700 ℃, roasting time 1～10 hour, preferred 1～5 hour, calcination atmosphere can carry out in air, nitrogen, carbon dioxide or ammonia atmosphere, also can give roasting under vacuum, catalyst after the roasting cools off naturally, promptly obtains the catalyst finished product.
Catalyst of the present invention is mainly used in the ethylene oxide hydration reaction, prepares industrial useful ethylene glycol product.Reaction raw materials is water and oxirane, and raw water is not had specific (special) requirements, can be the recirculated water in distilled water, deionized water, cooling water and this course of reaction.Make raw water and oxirane enter blender according to a certain percentage by measuring pump, enter preheater after fully mixing, raw material after the preheating enters in the fixed bed reactors that catalyst of the present invention is housed, reactor is the stainless steel tube of 8 millimeters of internal diameters, 300 millimeters of length, filler is housed up and down, reactor adopts the external heating mode heating, and 3 parallel thermocouples are equipped with control and measurement heating and reaction temperature in the outside.Reaction process condition: water is than 1～15: 1, and 100～200 ℃ of reaction temperatures, reaction pressure 0.5～3.0MPa, reactant liquor air speed 1.0～3.0 hours
-1, product obtains the ethylene glycol product through conventional partition method separation.
Solid acid catalyst of the present invention has good hydrothermal stability.With catalyst liquid air speed 50 hours
-1, pressure 3.0MPa carries out water-fast heat test in 1000 hours under 300 ℃ of conditions of temperature, conversion ratio and selectivity under the same process condition before and after the evaluate catalysts hydrothermal treatment consists.Find out by experimental data, catalyst is through after 1000 hours hydrothermal treatment consists, trend (embodiment 11) does not fall in conversion ratio and selectivity as follows, show that catalyst of the present invention is specially adapted to the inefficient high temperature aqueous reaction of general solid acid system, and have good reactivity worth and advantages of excellent stability.
Catalyst of the present invention is by the main active constituent of the conduct of load niobic acid on some oxide carriers, the compound that load is selected from IVA metallic compound, vib metal compound or its mixture and is selected from cerium, thorium is as co-catalyst, produce cooperative effect between each component, make the catalyst that makes have good reactivity worth, be used for ethylene oxide hydration and produce glycol reaction, have following advantage:
1, activity of such catalysts is good, and the selectivity height is 150 ℃ of reaction temperatures, reaction pressure 1.5MPa, water is than 1～10: 1, the liquid air speed was named under the process conditions and is prepared ethylene glycol in 1.0～3.0 hours, the oxirane conversion ratio reaches more than 98%, glycol selectivity about 90%.
2, operation water uses catalyst of the present invention can make reaction water than reduction significantly than low, and by the 20-25 of prior art: 1 reduces to 1～10: 1, reduced energy consumption significantly, and significantly reduce production costs.
3, catalyst reaction good stability, the life-span is long.But successive reaction is more than 1500 hours, and activity of such catalysts is not seen reduction, and the selectivity of ethylene glycol remains unchanged substantially, prolongs the catalyst runs cycle, reduces production costs.
4, solid acid catalyst of the present invention does not have corrosion to equipment, environmentally safe.
The present invention is further illustrated below by embodiment.
The specific embodiment
[embodiment 1]
With 10 gram niobic acids, 0.05 gram germanium dioxide and 100 gram α-Al
2O
3Fully mixed in kneading machine, add 50 milliliters in the rare nitric acid of weight concentration 1% and chromic nitrate (III) aqueous solution of 8.8 ml concns 0.03% (weight) then, mediate and form the bulk material, extruded moulding, in 100 ℃ of dryings 2 hours, roasting was 4 hours in 300 ℃ of air, obtains catalyst A.The catalyst composition sees Table 1.
[embodiment 2]
60 gram aluminium oxide and 40 gram silica are joined in the kneading machine, mix, add 60 milliliters in rare nitric acid of concentration 2% (weight) then, mediate to form the bulk material, extruded moulding was in 150 ℃ of dryings 2 hours, 1400 ℃ of roastings 4 hours, make the bar shaped carrier, carrier pulverized, with a certain amount of concentration be 125 mMs/liter ammonium molybdate aqueous solution at room temperature flood above-mentioned carrier, the maceration extract solid volume was than 2: 1, flooded 2 hours, elimination solution was in 120 ℃ of vacuum drying 2 hours; Weighing 12.5 gram niobic acids, 3.15 gram SnCl
22H
2O with soak molybdenum after carrier fully mix, add 70 milliliters of binding agent poly-vinyl alcohol solutions, and after mediate, after the extrusion, in 120 ℃ of vacuum drying 2 hours, roasting was 4 hours in 400 ℃ of ammonia atmospheres, obtained catalyst B.The catalyst composition sees Table 1.
[embodiment 3]
20.2 gram niobium oxalates, 100 gram SAPO-34 are joined in the kneading machine, add 55 milliliters of the aluminium colloidal sols of concentration 10% (weight) then, mediate and form the bulk material, extruded moulding, in 100 ℃ of dryings 2 hours, the bar shaped carrier was made in 600 ℃ of roastings 4 hours.With a certain amount of concentration 25 mMs/liter this catalyst precarsor of ammonium tungstate solution vacuum impregnation, liquid-solid volume ratio 2: 1 was flooded 2 hours, elimination solution in 120 ℃ of dryings 2 hours, obtains mixture 1.A certain amount of plumbi nitras is dissolved in water makes the aqueous solution and it is impregnated on the mixture 1, the maceration extract solid volume is than 1.5: 1, dip time 2 hours, elimination solution, in 120 ℃ dry 2 hours once more, roasting is 2 hours in 400 ℃ of air, obtains catalyst C.The catalyst composition sees Table 1.
[embodiment 4]
With SAPO-41, niobium ammonium complex compound (NH
4[NbO (C
2O
4)
2(H
2O)
2] (H
2O)
n), cerous nitrate fully mixes according to a certain percentage and join in the kneading machine, mix, add 60 milliliters in rare nitric acid of concentration 2% (weight) and 266 mMs/rise chromic nitrate (III) aqueous solution then, mediate and form the bulk material, extruded moulding, in 150 ℃ of vacuum drying 2 hours, 500 ℃ of vacuum bakings 4 hours obtained catalyst precursor 1; With a certain amount of concentration be 125 mMs/liter ammonium molybdate aqueous solution at room temperature flood above-mentioned carrier, the maceration extract solid volume was flooded 30 minutes than 1: 1, in 120 ℃ of dryings 2 hours, roasting was 2 hours in 500 ℃ of nitrogen atmospheres, obtains catalyst D.The catalyst composition sees Table 1.
[embodiment 5]
Take by weighing 65 gram aluminium oxide and 35 gram SAPO-34 powder join in the kneading machine, add 50 milliliters in rare nitric acid of concentration 8% (weight), mediate and form the bulk material, extruded moulding in 150 ℃ of dryings 2 hours, in 1000 ℃ of roastings 4 hours, is made the bar shaped carrier.Then it is crushed to 200 orders.Niobium oxalate is dissolved in the water, makes the niobium oxalate solution of concentration 0.07 grams per milliliter.Be impregnated on the carrier niobium oxalate is excessive, the maceration extract solid volume was flooded 2 hours than 2: 1, elimination solution, and 150 ℃ of dryings 2 hours obtain catalyst precursor 1.With 15 gram SnCl
22H
2O is dissolved in 70 milliliters of dilute hydrochloric acid solutions of concentration 10% (weight), makes stannous chloride solution, and with its excessive being impregnated on the catalyst precursor 1, the maceration extract solid volume is than 1.5: 1, dip time 30 minutes, elimination solution, 120 ℃ of vacuum drying 2 hours obtain presoma 2.Continue equivalent vacuum impregnation catalyst precursor 2 with the cerous nitrate aqueous solution, dip time 5 minutes, 120 ℃ of vacuum drying 2 hours once more in 400 ℃ of vacuum bakings 4 hours, obtain catalyst E.The catalyst composition sees Table 1.
[embodiment 6]
A certain amount of niobic acid, plumbi nitras, ammonium molybdate, 8 gram inorganic claies and 100 gram silica supports are joined in the kneading machine, mix, 65 milliliters in the rare nitric acid that adds concentration 3% (weight) then, mediate and form the bulk material, extruded moulding, drying is 2 hours in 120 ℃ of moving airs, and roasting is 4 hours in 200 ℃ of air.Obtain catalyst F.The catalyst composition sees Table 1.
[embodiment 7]
A certain amount of thorium nitrate (IV), cerous nitrate, niobic acid and alumina support are fully mixed, obtain solid mixture, then add 70 milliliters of 5% (weight) cyclodextrin solutions, behind kneading, extruded moulding, in 120 ℃ of vacuum drying 2 hours, 300 ℃ of vacuum bakings 2 hours obtain catalyst precursor 1.Then the method according to embodiment 5 is impregnated into stannous chloride on the catalyst precursor 1, and in 120 ℃ of vacuum drying 2 hours, roasting was 3 hours in 700 ℃ of carbon dioxide atmospheres, obtains catalyst G.The catalyst composition sees Table 1.
[embodiment 8]
100 gram silica supports are joined in the kneading machine, add 60 milliliters in rare nitric acid of concentration 4% (weight), mediate and form the bulk material, extruded moulding in 150 ℃ of dryings 2 hours, in 1000 ℃ of roastings 4 hours, is made the bar shaped carrier.Join in the kneader after carrier powder is broken to 200 orders, add a certain amount of niobic acid, thorium nitrate (IV), chromic nitrate (III), plumbi nitras then and mix, 60 milliliters of dilute nitric acid solutions that add concentration 2% (weight) again, mediate and form the bulk material, extruded moulding, in 120 ℃ of vacuum drying 2 hours, roasting was 3 hours in 400 ℃ of air, obtains catalyst H.The catalyst composition sees Table 1.
[embodiment 9]
100 gram aluminium oxide, 20 gram powdered graphites and a certain amount of plumbi nitras are joined fully mixing in the kneader, 60 milliliters of the dilute nitric acid solutions of adding concentration 2% (weight), mediate and form the bulk material, extruded moulding, 120 ℃ of dryings 2 hours, 1200 ℃ of roastings 4 hours obtain catalyst precursor 1, and it is crushed to 200 orders.Niobium ammonium complex compound (NH with the prescription requirement
4[NbO (C
2O
4)
2(H
2O)
2] (H
2O)
n), cerous nitrate, SnCl
22H
2O, 10 gram inorganic claies join in the kneader with presoma 1 and fully mix, add suitable quantity of water, fully kneading, and formation bulk material, extruded moulding, 120 ℃ of vacuum drying 2 hours, 300 ℃ of vacuum bakings 4 hours obtain catalyst I.The catalyst composition sees Table 1.
[embodiment 10]
Get each 10 milliliters of the catalyst A～I of embodiment 1～9 preparation, fill in 8 millimeters of internal diameters one by one, in long 300 millimeters the stainless steel fixed bed reactors, the filler of packing into up and down carries out the evaluation of catalyst.Use metering pump massage that than 1～10: 1 charging raw water and oxirane, reaction bed pressure is 1.5MPa, and 150 ℃ of reaction temperatures, liquid air speed are 2.0～3.0 hours
-1Prepared in reaction ethylene glycol under the condition carries out qualitative, quantitative analysis with the HP5890 gas-chromatography to product, ring oxidative ethane conversion ratio, glycol selectivity.Reaction result is listed in table 1.
[embodiment 11]
The test of catalyst tolerates hydrothermal stability.
Get 10 milliliters of the catalyst I of embodiment 9 preparation, be loaded into 8 millimeters of internal diameters, in long 300 millimeters the stainless steel fixed bed reactors, heat up, in reactor, feed water vapour, 300 ℃ of temperature, pressure 3.0MPa, air speed 50 hours
-1Under the condition, carry out hydrothermal test in 1000 hours, after the hydrothermal test, catalyst is handled without any regeneration, adopts and the preceding identical activity rating process conditions of hydrothermal treatment consists, investigates through the catalyst activity after the above-mentioned hydrothermal treatment consists.At reaction pressure 1.5MPa, 150 ℃ of reaction temperatures, water was than 10: 1, and the liquid air speed was named under the condition in 2.0 hours, carried out the catalyst activity evaluation; Reaction result is as follows:
Catalyst rings oxidative ethane conversion ratio % glycol selectivity %
Hydrothermal test preceding 99 93
After 1000 hours hydrothermal test 100 93
Through after 1000 hours hydrothermal test, trend does not fall in the conversion ratio of catalyst and selectivity as follows.
By above-mentioned same method, carry out the catalyst A of example 1 preparation and example 2 preparations the water-fast heat stabilization test of catalyst B, the conversion ratio and the selectivity of catalyst there is no downward trend, show that catalyst of the present invention has good hydrothermal stability.
[embodiment 12]
The catalyst reaction stability test.
Get 10 milliliters of the catalyst of embodiment 5 preparation, fill in 8 millimeters of internal diameters, in long 300 millimeters the stainless steel fixed bed reactors, the filler of packing into up and down carries out the catalyst stability test.With raw water and 10: 1 in molar ratio ratios of oxirane by the measuring pump charging, 150 ℃ of reaction temperatures, reaction pressure 1.5MPa, liquid air speed 3.0 hours
-1Prepared in reaction ethylene glycol under the condition carries out qualitative, quantitative analysis with the HP5890 gas-chromatography to product, ring oxidative ethane conversion ratio, glycol selectivity.Reaction was carried out 1500 hours continuously.Initial reaction stage, oxirane conversion ratio 100%, glycol selectivity 94% is reacted after 1500 hours oxirane conversion ratio 100%, glycol selectivity 94%.
Use catalyst of the present invention, trend does not fall in successive reaction 1500 hours, activity of such catalysts, selectivity as follows.
[comparative example 1]
With granularity is that to fill in internal diameter be 8 millimeters to 20-40 purpose porcelain ring 10ml, in long 300 millimeters the stainless steel fixed bed reactors, with raw water and oxirane your ratio of metering pump massage charging in 10: 1, at reaction pressure 1.5MPa, 150 ℃ of reaction temperatures, liquid air speed are 2.0 hours
-1Prepared in reaction ethylene glycol under the condition carries out qualitative, quantitative analysis with the HP5890 gas-chromatography to product, ring oxidative ethane conversion ratio, glycol selectivity.Reaction result is listed in table 1.
[comparative example 2]
Prepare ethylene glycol, difference according to the method identical with comparative example 1: raw material feed water ratio is 22: 1.Reaction result is listed in table 1.
Table 1
| The catalyst numbering | Catalyst is formed | Oxirane/water (mol ratio) | Air speed hour -1 | Oxirane conversion ratio % | Glycol selectivity % |
| A | 8％Nb 2O 5-0.05％GeO 2-0.4％Cr 2O 3/α-Al 2O 3 | 10 | 2.0 | 100 | 91 |
| B | 10％Nb 2O 5-2.1％SnO 2-3％MoO 3/60％Al 2O 3+40％SiO 2 | 7 | 3.0 | 100 | 92 |
| C | 5％Nb 2O 5-0.3％PbO 2-5％WO 3/SAPO-34 | 5 | 2.0 | 100 | 85 |
| D | 20％Nb 2O 5-0.7％Cr 2O 3-3.8％Ce 2O 3-1.6％MoO 3/ SAPO-41 | 2 | 3.0 | 100 | 83 |
| E | 13％Nb 2O 5-10％SnO 2-0.01％Ce 2O 3/65％SiO 2+35％ SAPO-34 | 10 | 3.0 | 100 | 94 |
| F | 15％Nb 2O 5-1.8％PbO 2-0.06％MoO 3/SiO 2 | 8 | 3.0 | 100 | 90 |
| G | 20％Nb 2O 5-15％SnO 2-0.04％-ThO 2-0.005％ Ce 2O 3/Al 2O 3 | 12 | 3.0 | 98 | 94 |
| H | 18％Nb 2O 5-0.2％PbO 2-0.08％-ThO 2+10％ Cr 2O 3/SiO 2 | 9 | 2.0 | 97 | 93 |
| I | 8％Nb 2O 5-5.2％SnO 2-1.0％PbO 2-0.001％ Ce 2O 3/Al 2O 3 | 10 | 2.0 | 99 | 93 |
| Compare 1 | / | 10 | 2.0 | 92 | 75.0 |
| Compare 2 | / | 22 | 2.0 | 100 | 90.0 |
Claims (8)
1, a kind ofly be used for the solid acid catalyst that ethylene oxide hydration is produced ethylene glycol, being selected from a kind of or its mixture in aluminium oxide, silica or the molecular sieve as carrier, the following active constituent of load on carrier, the percentage that accounts for vehicle weight is:
A) metal oxide of 5～20% niobiums;
B) 0.01～20% be selected from the metallic compound of IVA at least a;
C) 0.001～10% be selected from the metallic compound of VIB at least a;
D) 0～5% be selected from the metallic compound of cerium or thorium at least a.
2, according to the described solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol of claim 1, it is characterized in that in vehicle weight percentage the metal oxide consumption of niobium is 5～10%.
3, according to the described solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol of claim 1, it is characterized in that in vehicle weight percentage the metallic compound consumption that is selected from IVA is 0.05～15%.
4, according to the described solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol of claim 1, it is characterized in that in vehicle weight percentage the metallic compound consumption that is selected from VIB is 0.05～10%.
5, according to the described solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol of claim 1, it is characterized in that described aluminium oxide is an Alpha-alumina.
6, according to the described solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol of claim 1, it is characterized in that described molecular sieve is the SAPO molecular sieve.
7, according to the described solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol of claim 1, the metal that it is characterized in that described VIB is chromium, molybdenum or tungsten.
8, according to the described solid acid catalyst that is used for ethylene oxide hydration production ethylene glycol of claim 1, it is characterized in that described catalyst also contains binding agent, in vehicle weight percentage, the consumption of binding agent is 1～10%.
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