http://rdf.ncbi.nlm.nih.gov/pubchem/patent/ES-2328250-T3
Outgoing Links
| Predicate | Object |
|---|---|
| assignee | http://rdf.ncbi.nlm.nih.gov/pubchem/patentassignee/MD5_a5b5e06eec80c977b5bb7128cd57e763 |
| classificationCPCAdditional | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00891 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00889 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00873 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00835 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J2219-00783 |
| classificationCPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/B01J19-0093 http://rdf.ncbi.nlm.nih.gov/pubchem/patentcpc/C08G65-2696 |
| classificationIPCInventive | http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/B01J19-00 http://rdf.ncbi.nlm.nih.gov/pubchem/patentipc/C08G65-26 |
| filingDate | 2005-03-05-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| grantDate | 2009-11-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| inventor | http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_93d5228a060749b060349c8516c006a8 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_cf5ec4e1514b841e228896a509a712cf http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_09f69b057cfbf4c0f7fe453783429d16 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_442149b73e5dd06bac417beff0dc6d6d http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_aa4b1ba1e9bcdbda1d19f5deab6ec6e1 http://rdf.ncbi.nlm.nih.gov/pubchem/patentinventor/MD5_feb060728ccc710ee45ee9b58ea53b7f |
| publicationDate | 2009-11-11-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| publicationNumber | ES-2328250-T3 |
| titleOfInvention | ALCOXILATIONS IN MICROSTRUCTURED CAPILLARY REACTORS. |
| abstract | Process for the production of polyether alcohols of the general formula (I) ** see formula ** by alkoxylation of compounds of the general formula R 1 (XH) m in a microstructured reactor with series of channels connected in parallel for conducting chemical reactions between essentially liquid reaction partners, optionally in the presence of a solid catalyst, where the conduction of the chemical process takes place in spaces that are formed by two or more plates or layers of essentially parallel faces, in which the mixing of the reactants takes place individually in a single phase in a liquid state in each reaction channel and a heat exchanger device is provided, namely a cooling or heating device, and the reactor is designed for pressures up to 800 bar and temperatures in the range of - 30 ° C to 400 ° C, characterized in that the compound R 1 (XH) m and an appropriate catalyst is mixed n and introduced into the reactor, fed to the reactor 1 to 300, preferably 2 to 150 equivalents of alkylene oxide directly or at various points and mixed with the compound R 1 (XH) m, catalyst and / or its by-products, they are transformed into the reaction channels at a temperature in the range of 50 to 300 ° C and a pressure in the range of 11 to 800 bar and then the product mixture is cooled, where R 1 in the formula R 1 ( XH) m represents a mono- or polyvalent organic moiety, m represents a corresponding integer, R 2 is the same or different in the molecule and represents hydrogen and / or an organic moiety, particularly CH 3, C 2 H 5, phenyl, C 10 H 21, or allyloxymethyl, X represents O, S, NH or NR '', and R '' is a cyclic or acyclic organic moiety, optionally substituted with 1 to 26 carbon atoms. |
| priorityDate | 2004-03-19-04:00^^<http://www.w3.org/2001/XMLSchema#date> |
| type | http://data.epo.org/linked-data/def/patent/Publication |
Incoming Links
Total number of triples: 48.