HUE026365T2 - Eljárás kis szénatomszámú szénhidrogének elõállítására glicerinbõl - Google Patents
Eljárás kis szénatomszámú szénhidrogének elõállítására glicerinbõl Download PDFInfo
- Publication number
- HUE026365T2 HUE026365T2 HUE09744163A HUE09744163A HUE026365T2 HU E026365 T2 HUE026365 T2 HU E026365T2 HU E09744163 A HUE09744163 A HU E09744163A HU E09744163 A HUE09744163 A HU E09744163A HU E026365 T2 HUE026365 T2 HU E026365T2
- Authority
- HU
- Hungary
- Prior art keywords
- catalyst
- glycerol
- acrolein
- reactions
- reactor
- Prior art date
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
- C07C1/24—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms by elimination of water
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/20—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms
- C07C1/207—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms from carbonyl compounds
- C07C1/2076—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only oxygen atoms as heteroatoms from carbonyl compounds by a transformation in which at least one -C(=O)- moiety is eliminated
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/04—Ethylene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C11/00—Aliphatic unsaturated hydrocarbons
- C07C11/02—Alkenes
- C07C11/06—Propene
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/51—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition
- C07C45/52—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by pyrolysis, rearrangement or decomposition by dehydration and rearrangement involving two hydroxy groups in the same molecule
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C9/00—Aliphatic saturated hydrocarbons
- C07C9/02—Aliphatic saturated hydrocarbons with one to four carbon atoms
- C07C9/06—Ethane
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C9/00—Aliphatic saturated hydrocarbons
- C07C9/02—Aliphatic saturated hydrocarbons with one to four carbon atoms
- C07C9/08—Propane
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2521/00—Catalysts comprising the elements, oxides or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium or hafnium
- C07C2521/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- C07C2523/24—Chromium, molybdenum or tungsten
- C07C2523/30—Tungsten
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2523/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00
- C07C2523/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals
- C07C2523/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group C07C2521/00 of noble metals combined with metals, oxides or hydroxides provided for in groups C07C2523/02 - C07C2523/36
- C07C2523/56—Platinum group metals
- C07C2523/63—Platinum group metals with rare earths or actinides
Claims (4)
- Eljàrés kls szénaiomszémô szênhîdrogéoetc BlêâltMmm gieerinbôl SZäBäDäLMI mËWimmùK1. Epris két vagy hârom szénatomof tartalmazô szénhidrogèn eiôâilîtâsars gücerinböl ahol à szénhidrôgên osupan szénatomokat és hidroaénatomokat tsrtab ma|raNp| m eprés a kbvetkezô lépéseket tartalroazza; fiicarià hiztésltâsa; a glioerlnnek akroieinné valô konvertâlésa egy dehidrogénezési reakcîôkat katallzè-IÔ elsô katalizàîor aikalmazâssva!· és a iaiétkazei akrolainaak egy két vagy hérom szénatomot fariafmazo szénhidro-gènné valo konvertàiâsa, egy dekarbonlfezésl reakcîôkat kataîizâlô masodik kaiali-zàtor alkaimazâsé val, vagy egy hidrogénezési reakcîôkat katalizéio masodik kaiaii-zâtor VàiamM egy dehidratâlâsi reakcîôkat kalailzâlô harmadsk katafeâtor alkairna- zésâval. 2* Az 1 igènypont szerinii eljéras, amelyben a szénhidrogèn etân vagy etén, ès amelyben a mâsodik katalizétcr dekarhoniiezésl reakcîôkat katakzéi. ti A 2, igènypont szebnîi après, amelyben a szénhidrogèn etan, és amelyben a màsodik katailzâtert viz-gaz reakelot (VVGS), hidrogénezési és dekarbonHezêsi ré-akciôkat katalizéio kataîizétorok kbzel vélaszfjuk. 4, A 3. Igènypont szerlnti après, amelyben a masodik kafanzâior CeGron hordozott piétinât tartàlrnaz, §, Az elëzô igénypontok egylke szerinti eljàrés, amelyben az elsô és a mâso-dik kaiakzàtor egy elsô reaktorhao vaànak jelen, amely agy ès ugyanaz a reaktor. β. Az 1:.· igènypont szerlnti eljàrés, amely iovébbé magéban fogiap a követke-z6 fépèsekei: hidrogèn biztosltésa, aboi a szénhidrogèn propén vagy propèn, ès amelyben m mâsodik katafizâter bidrogénezési reakcîôkat kaiaüzal, ès a harmadik katalizâtor dehidratâlâsi reakciôkat katalIzâL 7, A 6. igènypont szerinti eljàrés, amelyben a szénhidrogèn propén, és amely-ben a hidrogént a gtiœrinre vonatkoztatva sziichiometrial felesieghen biztositjuk* 8* Az eiozô igénypontok egylke szerinti eljàrés, ameiyben a glicerint vtzzéi képzett elegykéni biztoslliuk, ès a giloerin koncenirédôja a glicehn ès viz elegyében 1-75 tômeg%. S. Ä 8. igénypont szerinis éliras, amelyben a glicarin/viz-elegy hôrnérsékiete. rendeikezèsre bocsatâskor 200-400^0, és amelyben a glicerint 280-400*0 hômér-sékfeton és 2-10 bar nyoméson konvertâljuk akrolelnné.
- 10, Az elozé igèîiypontok egyike szerinti eljäras, amelyben az elsé kaializàtor egy ZrOs-on hordozoti WOrQt tartalmazé savas katalizâtor.
- 11, Az 1, igénypont szerinti kaiaiizâtor, amelyben - a szénhidrogén etàn; - az also katalizâtor egy savas katalizâtor: - a mâsodik katalizâtor plaîlnât CeCVon hordozva iartaimazé katalizâtor; - a gHcerint egy vizze! képzeü eiegykén! biztositjuk, pèldâui olyan elegyként amelyben a gllcerin koncentracléja 15-30 tômeg%. - a homèrséktet, amelyen a gjjoennt akroleinné és az akroleinf etannâ konvertâljuk 28G-350°C; - a nyomés, amelyen a güeerlnt akroleinné és az akrolelnî etanné konvertâljuk 3,5-4,5 bar; - a glicerin/viz-eiegy rendélkezêsre bocsétéskori homérséfcteie 250-350*0; és - az elsö és a mäsodlk katallzàtor ugyanabban a reaktorban van jeien. 12, A 11. Igénypont szennti eljarés, amelyben az elso katalizâtor egy WOs-ot ir%-on hordozva tartalmazé savas katalizâtor.
- 13, Az 1-8. vagy 10. igénypont szennti eiiaràs, amelyben a szënbidrogén etén, és a mâsodik katalizâtor kataHzâlô elemkênt Pd/Cetb-ot tartalmazé katalizâtor. 14 Az 1. igénypont szerinti eljàras, amelyben: a güoerint vizzel képzett elegyként, gâzfàzlsban biztosftjuk, amely elegy hômérsékiete 2O0-40O°C; a glœrint skrolelnné 200-400X homérsékieien és 2-10 bar nyomàson konvertâljuk; az efârés tovâbbâ magiban foglaija hidrogènnek, glicerinre vonatkoztatva sztöchio-metrial feleslegben valô blztosttâsânak iépését; a szénhidrogén propân; és az akroleint az alàbbiak alkalmazasàval konvertâljuk propânnà: egy Wdrogénezèsi reakciokat kataHzâlô mâsodik katalizâtor, ameiy katalizâtor ZnÖ2-on hordozva îartaimaz rezsi amellyel az akroleint propanoilâ âlaklluft ât; egy harmadlk, dehidratalâsi reakolékat kaiskzâlo savas katalizâtor, amellyel a propanoit propénné alakitjuk ét; és egy negyedik, hidrogén&zési reakciokaf katalizélô katailzätor, ameJfyel a pro-pènt propt^né aiakftjuk àt. W, A 14v igènypont szerinîi eljârâs, amelyben a harmadîk feataHzâtor WO3-0I ZfC^oa hordoz^a fartalrnaz, és a negyedik katalizétor ê§f plafna-csoportbeli fêmet iartaimaxô kaiafeâio?
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11138808P | 2008-11-05 | 2008-11-05 | |
SE0850077 | 2008-11-14 |
Publications (1)
Publication Number | Publication Date |
---|---|
HUE026365T2 true HUE026365T2 (hu) | 2016-06-28 |
Family
ID=42125038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
HUE09744163A HUE026365T2 (hu) | 2008-11-05 | 2009-11-03 | Eljárás kis szénatomszámú szénhidrogének elõállítására glicerinbõl |
Country Status (12)
Country | Link |
---|---|
US (1) | US20110224470A1 (hu) |
EP (1) | EP2358653B1 (hu) |
CY (1) | CY1117044T1 (hu) |
DK (1) | DK2358653T3 (hu) |
ES (1) | ES2550788T3 (hu) |
HR (1) | HRP20151101T1 (hu) |
HU (1) | HUE026365T2 (hu) |
PL (1) | PL2358653T3 (hu) |
PT (1) | PT2358653E (hu) |
SI (1) | SI2358653T1 (hu) |
SM (1) | SMT201500259B (hu) |
WO (1) | WO2010052208A2 (hu) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US8692028B2 (en) | 2009-12-23 | 2014-04-08 | Biofuel-Solution I Malmo Ab | Method for hydrogenating 1,2-unsaturated carbonylic compounds |
EP2468709A1 (en) | 2010-11-30 | 2012-06-27 | BioFuel-Solution AB | A process for producing acrolein |
KR101629003B1 (ko) | 2013-11-18 | 2016-06-09 | 주식회사 엘지화학 | 글리세린 탈수반응용 촉매, 이의 제조 방법 및 아크롤레인의 제조 방법 |
WO2020117119A1 (en) | 2018-12-05 | 2020-06-11 | Biofuel-Solution I Malmö Ab | A process for converting glycerol to propane |
Family Cites Families (29)
Publication number | Priority date | Publication date | Assignee | Title |
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US3173959A (en) * | 1965-03-16 | Process for the production of saturated fatty alcohols | ||
US1895529A (en) * | 1926-06-24 | 1933-01-31 | Du Pont | Process of catalytic dehydration |
US2139351A (en) * | 1937-09-18 | 1938-12-06 | Shell Dev | Temperature control process and apparatus |
US3113986A (en) * | 1962-01-08 | 1963-12-10 | Hercules Powder Co Ltd | Hydrogenation of unsaturated hydrocarbons |
US3501546A (en) * | 1968-03-14 | 1970-03-17 | Ethyl Corp | Preparation of paraffinic hydrocarbons from acyclic,monohydric,primary alkanols and aldehydes having up to 24 carbon atoms with a catalyst consisting of palladium dispersed on titanium dioxide |
US3832392A (en) * | 1970-07-23 | 1974-08-27 | J Imamura | Process for producing perisobutyric acid |
US4049576A (en) * | 1974-10-04 | 1977-09-20 | Ashland Oil, Inc. | Platinum-palladium catalyst for selective hydrogenation of aromatics and olefins in hydrocarbon fractions |
US4032458A (en) * | 1975-08-08 | 1977-06-28 | Petro-Tex Chemical Corporation | Production of 1,4-butanediol |
US4036905A (en) * | 1976-04-12 | 1977-07-19 | Oxirane Corporation | Process for the manufacture of propylene oxide |
DE2810662C3 (de) * | 1978-03-11 | 1982-03-25 | Bayer Ag, 5090 Leverkusen | Verfahren zur Reinigung eines Epoxids oder eines solches enthaltenden Gemisches |
US4261700A (en) * | 1979-05-07 | 1981-04-14 | Colgate-Palmolive Company | Ignition method with pressure dispensable gelled fuel |
US5004845A (en) * | 1981-08-20 | 1991-04-02 | Davy Mckee (London) Limited | Hydrogenation of aldehydes |
GB8430223D0 (en) * | 1984-11-30 | 1985-01-09 | Exxon Research Engineering Co | Hydroformylation of olefins |
US4973792A (en) * | 1987-07-07 | 1990-11-27 | Uop | Chemical conversion process |
US4837367A (en) * | 1987-08-03 | 1989-06-06 | Eastman Kodak Company | Low pressure catalytic hydrogenation of carbonyl-containing compounds |
DE3932332A1 (de) * | 1989-09-28 | 1991-04-11 | Hoechst Ag | Verfahren zur herstellung von alkoholen (einstufig) |
IT1249955B (it) * | 1991-07-10 | 1995-03-30 | Menon S R L | Procedimento di idrogenazione della glicerina |
DE4238493C1 (de) * | 1992-11-14 | 1994-04-21 | Degussa | Verfahren zur Herstellung von Acrolein und dessen Verwendung |
US5865985A (en) * | 1997-02-14 | 1999-02-02 | Akzo Nobel Nv | Process for the production of diesel |
US5990323A (en) * | 1998-10-23 | 1999-11-23 | Eastman Chemical Company | Preparation of amines |
AU2001292696A1 (en) * | 2000-09-25 | 2002-04-08 | Engelhard Corporation | Suppression of methanation acitvity by a water gas shift reaction catalyst |
US7201783B2 (en) * | 2000-11-13 | 2007-04-10 | Idatech, Llc | Fuel processing system and improved feedstock therefor |
CA2485558C (en) * | 2002-05-10 | 2009-07-21 | Wisconsin Alumni Research Foundation | Low-temperature hydrocarbon production from oxygenated hydrocarbons |
US6960694B2 (en) * | 2003-07-01 | 2005-11-01 | Eastman Chemical Company | Processes for preparing β-hydroxy-ketones and α,β-unsaturated ketones |
KR101103212B1 (ko) * | 2003-09-18 | 2012-01-05 | 스미또모 가가꾸 가부시키가이샤 | 쿠멘의 제조 방법 |
JP4567961B2 (ja) * | 2003-11-27 | 2010-10-27 | 株式会社レボインターナショナル | 油脂からのデイーゼル燃料油製造プロセス |
US7585339B2 (en) * | 2004-09-15 | 2009-09-08 | Haldor Topsoe A/S | Process for reforming ethanol to hydrogen-rich products |
US7405337B2 (en) * | 2004-09-21 | 2008-07-29 | Uop Llc | Conversion of oxygenate to propylene with selective hydrogen treatment of heavy olefin recycle stream |
FR2882052B1 (fr) * | 2005-02-15 | 2007-03-23 | Arkema Sa | Procede de deshydratation du glycerol en acroleine |
-
2009
- 2009-11-03 US US13/127,599 patent/US20110224470A1/en not_active Abandoned
- 2009-11-03 DK DK09744163.8T patent/DK2358653T3/en active
- 2009-11-03 ES ES09744163.8T patent/ES2550788T3/es active Active
- 2009-11-03 PL PL09744163T patent/PL2358653T3/pl unknown
- 2009-11-03 EP EP09744163.8A patent/EP2358653B1/en not_active Not-in-force
- 2009-11-03 WO PCT/EP2009/064517 patent/WO2010052208A2/en active Application Filing
- 2009-11-03 PT PT97441638T patent/PT2358653E/pt unknown
- 2009-11-03 SI SI200931291T patent/SI2358653T1/sl unknown
- 2009-11-03 HU HUE09744163A patent/HUE026365T2/hu unknown
-
2015
- 2015-10-19 HR HRP20151101TT patent/HRP20151101T1/hr unknown
- 2015-10-22 SM SM201500259T patent/SMT201500259B/it unknown
- 2015-10-22 CY CY20151100946T patent/CY1117044T1/el unknown
Also Published As
Publication number | Publication date |
---|---|
ES2550788T3 (es) | 2015-11-12 |
SMT201500259B (it) | 2016-01-08 |
PL2358653T3 (pl) | 2016-01-29 |
EP2358653B1 (en) | 2015-07-22 |
US20110224470A1 (en) | 2011-09-15 |
WO2010052208A2 (en) | 2010-05-14 |
DK2358653T3 (en) | 2015-10-26 |
HRP20151101T1 (hr) | 2015-12-04 |
PT2358653E (pt) | 2015-11-16 |
CY1117044T1 (el) | 2017-04-05 |
WO2010052208A3 (en) | 2010-07-22 |
SI2358653T1 (sl) | 2015-12-31 |
EP2358653A2 (en) | 2011-08-24 |
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