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DE845937C - Process for the preparation of alkylene oxides - Google Patents

Process for the preparation of alkylene oxides

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Publication number
DE845937C
DE845937C DEB7399D DEB0007399D DE845937C DE 845937 C DE845937 C DE 845937C DE B7399 D DEB7399 D DE B7399D DE B0007399 D DEB0007399 D DE B0007399D DE 845937 C DE845937 C DE 845937C
Authority
DE
Germany
Prior art keywords
preparation
alkylene oxides
oxides
heated
inert gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
DEB7399D
Other languages
German (de)
Inventor
Otto Dr Roser
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BASF SE
Original Assignee
BASF SE
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Priority to DEB7399D priority Critical patent/DE845937C/en
Application granted granted Critical
Publication of DE845937C publication Critical patent/DE845937C/en
Expired legal-status Critical Current

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  • Paints Or Removers (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Description

Verfahren zur Herstellung von Alkylenoxyden Ks wttr(leeflinden. (1a1.1 111,111 :\Ihvlcih)X-v(k. iit eiiifacltercise t111(1 ittit "titer.@usl)et;te erliält.weiiii matt x-( A vl:()lhohlcnsüureest(r. die z. 1i. durch C'ni- :etztiii- vOH ()letitthal()rnhv(lrittcil mit Natrium- 1)icarh()nat er'll:iltlich sind. erhitzt. Vorteilhaft \ertveil(let malt "I'e#ml)eraturen zwischen loo tilid -oc) : dir ( ilvl:()Ik()lllensüurecster. z. I). die Kohleil- s:iurees@ur dus :\tilvleit- oder- 1'ropylcitnlyko1s. sl)alteit :ich (lal)ci in .@ll:@l(ilowc@ uitd Kohlen- (li()xv(1. 1)1c z(,1-setztlll", die lxci @;ewühulichem (xler crinedrigtetn Druck vor sich rieht. kann in Gegen- wart von Ill'at:tlvstttoreii, z. 1;. \letallomyden. wie I:i:enowrl, @illkroxwl, \icl:elmd, oder \letall- Salzetl, wie Sill>ercarl)onat, oder ol>erljäcl@nakti@en Stoffett, wie Kieselgel, Aktivkohle 1i. d61.. durrh- riefiiltrt tverden. l)as erhaltene _\Ikylenowd kaiiri, 1>fisl»elsweise durch Kondensation, teilweise oder \-ii'li<l; v(111 dein f@ohlendit>s_v<i abgetrennt und rein erhalten werden. \1a11 1:a1111 (lie erhaltenen _@ll:v@enoxvd-lioh@en- ::iure-(icmi:cltt mich unmittelbar (>(ler. nach teil- we@ser I..lltfcriltiti" (>der nach Zugabc Not, _\lkvIell- owd beispielsweise für @uhädlin@strekä ml)fungs- zweckr. verwett(len. 1)a die Herstellung der .\1- kylenoxyde bzw. ihrer Gemische mit Kohlensäure: aus den leicht versandfähigen a-Glykolkohlensäure- estern sehr einfach ist, kann sie am Ort der Ver- wendung erfolgen, wodurch der Transport solcher Gemische, der in Druckgefäßen geschehen maß, entbehrlich wird. Die bekannte Herstellung von :@Iki-lenoxyden aus Halogenhvdrinen. I>ei cler stets Ahfallprodukte entstehen, bietet diesen \'oi-teil nicht, da sie in Fabrikationsanlagen durchgeführt werden maß. Beispiel i ioo Gewichtsteile Äthy-lenglykolkolilensiitireestei- «-erden in einem inerten Gasstrom, z. 13. Kohlen- dioxyd oder Stickstoff, auf 200° erwärmt. Es tritt lebhafte Zersetzung ein. Die Gase werden durch eilte etwas unter o" gekühlte Vorlage geleitet, wo- bei sich etwa lo (@et@ichtsteile Äthvlenot@-d flüssig abscheiden. Beispiel 2 ioo Gewichtsteile Äth vlenglyk@>lkohlens:ittreester werden unter 7usatz von etwa 5 GcH-iclitsteileii Silberoxyd auf etm-a ioo° erhitzt. hierbei tritt lebhafte Zersetzung inth@ lenoxyd arid Kolik@ti- süure ein. Die Aasheute an tltht letuixi-tl 1>etr ügt etwa 1o ( @ewicbtsteile. Beispiel 3 Nlan erhitzt Ätliyleiiglykolkolilciis:itii-eester auf 21o° und fängt das in einer \leige voii ettv-a <So°'o der Theorie gebildete @ti@lciio@vd iii einer mit Fis gekühlten Vorlage auf oder verwendet (las eiit- stehetide Gemisch von Äthi-lcnosv(1 mit l@ii'lileii- dioxyd urimittelbar für die Sch@i<ililigslx-küntlifulig. Process for the preparation of alkylene oxides Ks wttr (leeflinden. (1a1.1 111,111 : \ Ihvlcih) Xv (k. Iit eiiifacltercise t111 (1 ittit "titer. @ usl) et; te erliält.weiiii matt x- ( A vl :() hollow acid residue (r. the z. 1i. by C'ni- : etztiii- v OH () letitthal () rnhv (lrittcil with sodium 1) icarh () nat er'll: are iltlich. heated. Advantageous \ ertveil (let paints "I'e # ml) eratures between loo tilid -oc): dir (ilvl :() Ik () lllensüurecster. z. I). the coal s: iurees @ ur dus: \ tilvleit- or- 1'ropylcitnlyko1s. sl) alteit: i (lal) ci in. @ ll: @l (ilowc @ uitd coal (li () xv (1. 1) 1c z (, 1-setslll ", the lxci @; ewühulichem (xler crinedrigtetn pressure in front of him. can in counter wart von Ill'at: tlvstttoreii, z. 1;. \ letallomyden. how I: i: enowrl, @illkroxwl, \ icl: elmd, or \ letall- Salzetl, like Sill> ercarl) onat, or ol> erljäcl @ nakti @ en Stoffett, such as silica gel, activated carbon 1i. d61 .. durrh- called iiltrt tverden. l) as preserved _ \ Ikylenowd kaiiri, 1> fisl »el wise by condensation, partially or \ -ii'li <l; v (111 your f @ ohlendit> s_v <i can be separated and kept pure. \ 1a11 1: a1111 (lie received _ @ ll: v @ enoxvd-lioh @ en- :: iure- (icmi: cltt me immediately (> (ler. after part- we @ ser I..lltfcriltiti "(> the one after adding Not, _ \ lkvIell- owd e.g. for @ uhädlin @ strekä ml) fungs- purposeful bet (len. 1) a the production of the. \ 1- kylene oxides or their mixtures with carbonic acid: from the easily dispatchable a-glycolic acid estern is very simple, it can be done at the application, which means the transport of such Mixtures that happened in pressure vessels, becomes dispensable. The well-known manufacture of : @ Iki-lenoxides from Halogenhvdrinen. I> ei cler always This \ 'oi part is created by waste products not because they are carried out in manufacturing plants are measured. Example i 100 parts by weight of Ethy-Lenglykolilensiitireestei- «-Erden in an inert gas stream, e.g. 13. Coal dioxide or nitrogen, heated to 200 °. It kicks vigorous decomposition. The gases are through hurried something under o "cooled template, where- with itself about lo (@ et @ ichtsteile Äthvlenot @ -d liquid deposit. Example 2 100 parts by weight of Äth vlenglyk @> lkohlens: ittreester are added with about 5 GcH-iclitteileii Silver oxide heated to etm-a 100 °. here occurs lively decomposition inth @ lenoxyd arid Kolik @ ti- süure a. The carrion today an tltht letuixi-tl 1> etr ughs about 1o (@ewicbtsteile. Example 3 Nlan heated Ätliyleiiglykolkolilciis: itii-eester on 21o ° and begins in a \ leige voii ettv-a <So ° 'o @ ti @ lciio @ vd iii one with F sharp cooled template on or used (read standing mixture of ethi-lcnosv (1 with l @ ii'lileii- Dioxyd urimittelbar for the Sch @ i <ililigslx-küntlifulig.

Claims (1)

PATENTANSPRÜCHE: i. Verfahren zur llerstelltitig \()n :\lke@en- oxyden,dadurch gekennzeichnet, daß man a-Glv- kolkohlensäureester unter ge@c@ilnllichem oder vermindertem Druck erhitzt, vorzugsweise auf Temperaturen zwischen ioo tin(1 200`. 2. Verfahren nach :lnsprnch i, dadurch ge- kennzeichnet, daß das Et-hitzeti iti einem inerten Gasstrom erfolgt. 3. Verfahren nach Anspruch 1 Lidei" 2, (h1- durch gekennzeiclitiet. (laß statt in ( @egen@@-art von Katalysatoren arbeitet.
Angezogene l)ruchscliriftcit: USA.-Patentschrift f\ r. t 9f>7 433: französische Patentschrift \r. 73o`(@d: deutsche l'atetitsclii-ift \r. ;41 7()t).
PATENT CLAIMS: i. Procedure for creating \ () n: \ lke @ en- oxides, characterized in that a-Glv- carbonic acid esters under common or heated under reduced pressure, preferably to Temperatures between ioo tin (1 200`. 2. Method according to: lnsprnch i, thereby indicates that the Et-hitzeti is an inert Gas flow takes place. 3. The method according to claim 1 Lidei "2, (h1- by gekennzeiclitiet. (instead of in (@egen @@ - art of catalysts works.
Dressed l) smell cliriftcit: USA. Patent for. t 9f> 7 433: French patent specification \ r. 73o` (@d: german l'atetitsclii-ift \ r. ; 41 7 ( ) t).
DEB7399D 1939-04-02 1939-04-02 Process for the preparation of alkylene oxides Expired DE845937C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
DEB7399D DE845937C (en) 1939-04-02 1939-04-02 Process for the preparation of alkylene oxides

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Application Number Priority Date Filing Date Title
DEB7399D DE845937C (en) 1939-04-02 1939-04-02 Process for the preparation of alkylene oxides

Publications (1)

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DE845937C true DE845937C (en) 1952-08-07

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Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2851469A (en) * 1958-09-09 Manufacture of ethylene oxide
US2856413A (en) * 1956-07-23 1958-10-14 Jefferson Chem Co Inc Method for preparing glycidol
US2924607A (en) * 1957-10-18 1960-02-09 Du Pont Preparation of oxetanes
US2985666A (en) * 1961-05-23 Process for the manufacture of
US4111965A (en) * 1974-04-10 1978-09-05 Phillips Petroleum Company Preparation of vicinal epoxides
US4257966A (en) * 1978-08-17 1981-03-24 Phillips Petroleum Company Preparation of vicinal epoxides
US4266046A (en) * 1976-09-17 1981-05-05 Phillips Petroleum Company Esterification process
US4276223A (en) * 1979-09-10 1981-06-30 Phillips Petroleum Company Preparation of vicinal epoxides
EP0047474A1 (en) * 1980-09-04 1982-03-17 Union Carbide Corporation Process for the preparation of epoxides from alkylene carbonates
EP0047473A1 (en) * 1980-09-04 1982-03-17 Union Carbide Corporation Process for the preparation of epoxides from alkylene carbonates
WO2009153194A1 (en) * 2008-06-18 2009-12-23 Basf Se Method for producing glycidyl esters

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE541769C (en) * 1927-07-12 1932-01-18 Ag Th Goldschmidt Process for the preparation of alkylene oxides from alkylene chlorohydrins
FR730864A (en) * 1931-02-10 1932-08-25 Anglo Persian Oil Company Ltd Improvements in the production of ethylene oxide
US1967433A (en) * 1934-07-24 Hydro-aromatic oxides

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1967433A (en) * 1934-07-24 Hydro-aromatic oxides
DE541769C (en) * 1927-07-12 1932-01-18 Ag Th Goldschmidt Process for the preparation of alkylene oxides from alkylene chlorohydrins
FR730864A (en) * 1931-02-10 1932-08-25 Anglo Persian Oil Company Ltd Improvements in the production of ethylene oxide

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2851469A (en) * 1958-09-09 Manufacture of ethylene oxide
US2985666A (en) * 1961-05-23 Process for the manufacture of
US2856413A (en) * 1956-07-23 1958-10-14 Jefferson Chem Co Inc Method for preparing glycidol
US2924607A (en) * 1957-10-18 1960-02-09 Du Pont Preparation of oxetanes
US4111965A (en) * 1974-04-10 1978-09-05 Phillips Petroleum Company Preparation of vicinal epoxides
US4266046A (en) * 1976-09-17 1981-05-05 Phillips Petroleum Company Esterification process
US4257966A (en) * 1978-08-17 1981-03-24 Phillips Petroleum Company Preparation of vicinal epoxides
US4276223A (en) * 1979-09-10 1981-06-30 Phillips Petroleum Company Preparation of vicinal epoxides
EP0047474A1 (en) * 1980-09-04 1982-03-17 Union Carbide Corporation Process for the preparation of epoxides from alkylene carbonates
EP0047473A1 (en) * 1980-09-04 1982-03-17 Union Carbide Corporation Process for the preparation of epoxides from alkylene carbonates
WO2009153194A1 (en) * 2008-06-18 2009-12-23 Basf Se Method for producing glycidyl esters
CN102066349A (en) * 2008-06-18 2011-05-18 巴斯夫欧洲公司 Method for producing glycidyl esters
US8236974B2 (en) 2008-06-18 2012-08-07 Basf Se Process for preparing glycidyl esters
CN102066349B (en) * 2008-06-18 2013-11-27 巴斯夫欧洲公司 Process for preparing glycidyl esters

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