HRP20200358T1 - Postupak pripreme etilen glikola - Google Patents

Postupak pripreme etilen glikola Download PDF

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Publication number
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
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Croatia
Prior art keywords
preparation
tungsten
diol
parts
diol according
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HRP20200358TT
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English (en)
Inventor
Jing Liu
Hongbin Qi
Haiyu Ren
Indra Prakash
Yu Shi
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Changchun Meihe Science and Technology Development Co., LTD.
The Coca-Cola Company
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Publication of HRP20200358T1 publication Critical patent/HRP20200358T1/hr

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/001Controlling catalytic processes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts 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
    • B01J23/835Catalysts 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
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts 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
    • B01J23/84Catalysts 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
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/888Tungsten
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76Catalysts 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
    • B01J23/84Catalysts 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
    • B01J23/85Chromium, molybdenum or tungsten
    • B01J23/888Tungsten
    • B01J23/8885Tungsten containing also molybdenum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J25/00Catalysts of the Raney type
    • B01J25/02Raney nickel
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J27/00Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14Phosphorus; Compounds thereof
    • B01J27/186Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • B01J27/19Molybdenum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00Catalysts, in general, characterised by their form or physical properties
    • B01J35/19Catalysts containing parts with different compositions
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/04Mixing
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/132Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/60Preparation 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
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C31/00Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
    • C07C31/18Polyhydroxylic acyclic alcohols
    • C07C31/20Dihydroxylic alcohols
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C31/00Saturated compounds having hydroxy or O-metal groups bound to acyclic carbon atoms
    • C07C31/18Polyhydroxylic acyclic alcohols
    • C07C31/20Dihydroxylic alcohols
    • C07C31/202Ethylene glycol
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00017Controlling the temperature
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008Controlling the process
    • B01J2208/00539Pressure
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/16Catalysts 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
    • B01J23/24Chromium, molybdenum or tungsten
    • B01J23/30Tungsten
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2523/00Constitutive chemical elements of heterogeneous catalysts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J37/00Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
    • B01J37/0081Preparation by melting
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/582Recycling 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.
HRP20200358TT 2014-09-28 2020-03-03 Postupak pripreme etilen glikola HRP20200358T1 (hr)

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

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HRP20200358T1 true HRP20200358T1 (hr) 2020-08-07

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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)

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CN102020531A (zh) 2010-10-20 2011-04-20 华东理工大学 一种低碳多元醇的制备方法
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CN102643165B (zh) 2011-06-28 2014-07-02 中国科学院大连化学物理研究所 连续加氢裂解糖转化生产乙二醇及1,2-丙二醇的方法
CN103608320A (zh) 2011-07-28 2014-02-26 环球油品公司 由糖类生产多元醇
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CN103159587A (zh) 2011-12-08 2013-06-19 中国科学院大连化学物理研究所 一种催化剂在生物多元醇加氢裂解中的应用
CN103420798B (zh) * 2012-05-18 2015-12-09 中国科学院大连化学物理研究所 一种高效催化转化纤维素类原料到二元醇的方法
CN103420787B (zh) 2012-05-21 2015-01-28 中国科学院大连化学物理研究所 近或超临界水条件下碳水化合物制小分子多元醇的方法
CN103420796B (zh) 2012-05-21 2015-05-20 中国科学院大连化学物理研究所 一种高金属负载量催化剂用于碳水化合物制乙二醇的方法
CN103420797B (zh) 2012-05-21 2015-04-08 中国科学院大连化学物理研究所 低金属负载量催化剂用于碳水化合物制备乙二醇的方法
CN102731258B (zh) * 2012-05-21 2014-07-23 中国科学院大连化学物理研究所 一种碳水化合物内循环催化转化制备低碳多元醇的方法
CN102731259A (zh) 2012-06-26 2012-10-17 北京大学 Cu基负载型催化剂在高碳多元醇选择氢解制备低碳二元醇中的应用
CN103667365A (zh) 2012-08-31 2014-03-26 郸城财鑫糖业有限责任公司 一种农作物秸秆制备二元醇的方法
CN103848720B (zh) * 2012-12-05 2015-08-26 中国科学院大连化学物理研究所 一种制备乙二醇的方法
CN106573860B (zh) 2014-04-09 2020-10-27 马来西亚国家石油公司 含糖类的原料选择性转化为乙二醇的方法
CA2949512C (en) * 2014-05-19 2020-08-18 Iowa Corn Promotion Board Process for the continuous production of ethylene glycol from carbohydrates
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

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