HRP20200358T1 - Postupak pripreme etilen glikola - Google Patents
Postupak pripreme etilen glikola Download PDFInfo
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- HRP20200358T1 HRP20200358T1 HRP20200358TT HRP20200358T HRP20200358T1 HR P20200358 T1 HRP20200358 T1 HR P20200358T1 HR P20200358T T HRP20200358T T HR P20200358TT HR P20200358 T HRP20200358 T HR P20200358T HR P20200358 T1 HRP20200358 T1 HR P20200358T1
- Authority
- HR
- Croatia
- Prior art keywords
- preparation
- tungsten
- diol
- parts
- diol according
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims 15
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 title claims 6
- 150000002009 diols Chemical class 0.000 claims 15
- 239000003054 catalyst Substances 0.000 claims 6
- WFKWXMTUELFFGS-UHFFFAOYSA-N tungsten Chemical compound [W] WFKWXMTUELFFGS-UHFFFAOYSA-N 0.000 claims 5
- 229910052721 tungsten Inorganic materials 0.000 claims 5
- 239000010937 tungsten Substances 0.000 claims 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 3
- ZOKXTWBITQBERF-UHFFFAOYSA-N Molybdenum Chemical compound [Mo] ZOKXTWBITQBERF-UHFFFAOYSA-N 0.000 claims 3
- 239000002253 acid Substances 0.000 claims 3
- 229910052739 hydrogen Inorganic materials 0.000 claims 3
- 239000001257 hydrogen Substances 0.000 claims 3
- 229910052750 molybdenum Inorganic materials 0.000 claims 3
- 239000011733 molybdenum Substances 0.000 claims 3
- 239000007858 starting material Substances 0.000 claims 3
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims 2
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 claims 2
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 claims 2
- 239000000956 alloy Substances 0.000 claims 2
- 229910045601 alloy Inorganic materials 0.000 claims 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims 2
- 229910052782 aluminium Inorganic materials 0.000 claims 2
- 229910052796 boron Inorganic materials 0.000 claims 2
- 150000002016 disaccharides Chemical class 0.000 claims 2
- 150000004676 glycans Chemical class 0.000 claims 2
- 150000002772 monosaccharides Chemical class 0.000 claims 2
- 229910052759 nickel Inorganic materials 0.000 claims 2
- 229920001542 oligosaccharide Polymers 0.000 claims 2
- 150000002482 oligosaccharides Chemical class 0.000 claims 2
- 229910052698 phosphorus Inorganic materials 0.000 claims 2
- 239000011574 phosphorus Substances 0.000 claims 2
- 229920001282 polysaccharide Polymers 0.000 claims 2
- 239000005017 polysaccharide Substances 0.000 claims 2
- 229910052761 rare earth metal Inorganic materials 0.000 claims 2
- 229910052718 tin Inorganic materials 0.000 claims 2
- ZNOKGRXACCSDPY-UHFFFAOYSA-N tungsten trioxide Chemical compound O=[W](=O)=O ZNOKGRXACCSDPY-UHFFFAOYSA-N 0.000 claims 2
- CMPGARWFYBADJI-UHFFFAOYSA-L tungstic acid Chemical compound O[W](O)(=O)=O CMPGARWFYBADJI-UHFFFAOYSA-L 0.000 claims 2
- ZGRBQKWGELDHSV-UHFFFAOYSA-N N.[W+4] Chemical compound N.[W+4] ZGRBQKWGELDHSV-UHFFFAOYSA-N 0.000 claims 1
- UMDRMROWMVLIJP-UHFFFAOYSA-N P(=O)(=O)[W].[Na] Chemical compound P(=O)(=O)[W].[Na] UMDRMROWMVLIJP-UHFFFAOYSA-N 0.000 claims 1
- CZIMGECIMULZMS-UHFFFAOYSA-N [W].[Na] Chemical compound [W].[Na] CZIMGECIMULZMS-UHFFFAOYSA-N 0.000 claims 1
- 239000002131 composite material Substances 0.000 claims 1
- 150000001875 compounds Chemical class 0.000 claims 1
- 230000035484 reaction time Effects 0.000 claims 1
- 150000003839 salts Chemical class 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- 150000003658 tungsten compounds Chemical class 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
- B01J8/001—Controlling catalytic processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/835—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with germanium, tin or lead
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/84—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/85—Chromium, molybdenum or tungsten
- B01J23/888—Tungsten
- B01J23/8885—Tungsten containing also molybdenum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J25/00—Catalysts of the Raney type
- B01J25/02—Raney nickel
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- B01J27/14—Phosphorus; Compounds thereof
- B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
- B01J27/19—Molybdenum
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/19—Catalysts containing parts with different compositions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/04—Mixing
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- 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
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- 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
- C07C29/132—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 an oxygen containing functional group
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- 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
- C07C29/60—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by elimination of -OH groups, e.g. by dehydration
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/18—Polyhydroxylic acyclic alcohols
- C07C31/20—Dihydroxylic alcohols
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C31/00—Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
- C07C31/18—Polyhydroxylic acyclic alcohols
- C07C31/20—Dihydroxylic alcohols
- C07C31/202—Ethylene glycol
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00017—Controlling the temperature
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
- B01J2208/00008—Controlling the process
- B01J2208/00539—Pressure
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/24—Chromium, molybdenum or tungsten
- B01J23/30—Tungsten
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2523/00—Constitutive chemical elements of heterogeneous catalysts
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0081—Preparation by melting
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/582—Recycling of unreacted starting or intermediate materials
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Catalysts (AREA)
Claims (13)
1. Postupak za pripremu diola, naznačen time što postupak koristi šećer i vodik kao polazišne materijale koji se dovode u kontakt s katalizatorom u vodi za pripremu diola; korišteni katalizator je kompozitni katalizator, koji se sastoji od glavnog katalizatora i kokatalizatora,
pri čemu
glavni katalizator je u vodi netopiva legura otporna na kiseline koja se sastoji od nikla, jednog ili više rijetkih zemljanih elemenata, kositar i aluminij i izborno i) volfram, ii) volfram i molibden, ili iii) volfram, molibden i bor ili fosfor;
kokatalizator je topiva sol volframske kiseline i / ili netopivi volframov spoj; diol je etilen glikol; i reakcijski sustav pH je 1 - 7.
2. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što je šećer odabran između jednog ili više monosaharida sa pet ugljika, disaharida i oligosaharida, monosaharida sa šest ugljika, disaharida i oligosaharida, topivog polisaharida sa pet ugljika i topivog polisaharida sa šest ugljika.
3. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što šećer reagira s vodikom u obliku vodene otopine šećera, i polazni materijal vodene otopine šećera ima koncentraciju 5 - 60 mas.%.
4. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što se legura otporna na kiselinu sastoji od, u dijelovima po masi, 10 - 90 dijelova nikla, 1 - 5 dijelova rijetkih zemljanih elemenata, 1 - 60 dijelova kositra i 5 - 9 dijelova aluminija i, kada su prisutni, 1-90 dijelova volframa, 0.5-20 dijelova molibdena, i 0.01-5 dijelova bora ili fosfora.
5. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što sol topive volframske kiseline je jedan ili više od amonijevog volframa, natrijevog volframa i natrijevog fosfovolframa.
6. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što je netopivi volframov spoj volfram trioksid i / ili volframova kiselina.
7. Postupak za pripremu diola prema patentnom zahtjevu 3, naznačen time što se kokatalizator dodaje otopini šećera prije dodavanja u reaktor, i pri čemu je količina upotrijebljenog topivog kokatalizatora 0.01 - 5 mas.% vodene otopine šećera.
8. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što reakcijski sustav ima reakcijski tlak 5 - 12 MPa, reakcijsku temperaturu od 150 do 260 ° C, i vrijeme reakcije > 10 min.
9. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što je reakcija u kontinuiranom stanju.
10. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što kokatalizator već otopljen u reakcijskom sustavu se odvaja od proizvoda i zatim reciklira.
11. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što se reakcija odvija u reaktoru suspenzijskog sloja.
12. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što šećer reagira s vodikom u obliku vodene otopine šećera, i polazni materijal vodene otopine šećera ima koncentraciju 20-50 mas.%.
13. Postupak za pripremu diola prema patentnom zahtjevu 1, naznačen time što je glavni katalizator odabran između grupa koja se sastoji od Ni80La1Sn30Al5;
Ni10Sm5Sn3Al9W70Mo5;
Ni70Ce1Sn50Al7W5Mo1B5;
Ni90Ce3Sn60Al9W20Mo5B1;
Ni10Sm5Sn10Al9W90;
Ni90Ce3Sn60Al9W20Mo20P0.01 i
Ni80La1Ce0.5Sn30Al5.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201410512704.7A CN105523890B (zh) | 2014-09-28 | 2014-09-28 | 一种制备二元醇的方法 |
PCT/CN2015/090321 WO2016045583A1 (zh) | 2014-09-28 | 2015-09-23 | 一种制备二元醇的方法 |
EP15844083.4A EP3199512B1 (en) | 2014-09-28 | 2015-09-23 | Method for preparing ethylene glycol |
Publications (1)
Publication Number | Publication Date |
---|---|
HRP20200358T1 true HRP20200358T1 (hr) | 2020-08-07 |
Family
ID=55580318
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
HRP20200358TT HRP20200358T1 (hr) | 2014-09-28 | 2020-03-03 | Postupak pripreme etilen glikola |
Country Status (18)
Country | Link |
---|---|
US (4) | US10464870B2 (hr) |
EP (2) | EP3199512B1 (hr) |
KR (2) | KR102601107B1 (hr) |
CN (2) | CN105523890B (hr) |
AU (2) | AU2015320134B2 (hr) |
CA (1) | CA2966521C (hr) |
DK (1) | DK3199512T3 (hr) |
EA (1) | EA035720B1 (hr) |
ES (1) | ES2779549T3 (hr) |
HR (1) | HRP20200358T1 (hr) |
HU (1) | HUE048744T2 (hr) |
MY (2) | MY197089A (hr) |
PL (1) | PL3199512T3 (hr) |
PT (1) | PT3199512T (hr) |
RU (1) | RU2698724C2 (hr) |
SI (1) | SI3199512T1 (hr) |
WO (1) | WO2016045583A1 (hr) |
ZA (1) | ZA201702942B (hr) |
Families Citing this family (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111545213B (zh) | 2014-09-28 | 2023-08-04 | 长春美禾科技发展有限公司 | 一种耐酸合金催化剂 |
CN105523890B (zh) * | 2014-09-28 | 2021-04-16 | 长春美禾科技发展有限公司 | 一种制备二元醇的方法 |
EP3245181B1 (en) | 2015-01-13 | 2019-10-23 | Avantium Knowledge Centre B.v. | Continuous process for preparing ethylene glycol from a carbohydrate source |
CN106694009B (zh) * | 2015-11-12 | 2019-12-13 | 中国科学院大连化学物理研究所 | 合金催化剂用于碳水化合物催化制备低碳二元醇的方法 |
CN109641191B (zh) * | 2016-06-03 | 2023-04-04 | 爱荷华谷类推广协会 | 将产生己醛糖的碳水化合物高度选择性地转化为乙二醇的连续方法 |
CN106349014B (zh) * | 2016-08-23 | 2020-08-18 | 上海交通大学 | 利用乙酰丙酸酯制备1,4-戊二醇的方法 |
CN110072834A (zh) * | 2016-12-19 | 2019-07-30 | 国际壳牌研究有限公司 | 在二醇生产中稳定葡萄糖进料的方法 |
CN109107581A (zh) * | 2017-06-22 | 2019-01-01 | 长春美禾科技发展有限公司 | 一种耐酸合金催化剂 |
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