Novel gemini surfactant and their use
US-2016368863-A1 · Dec 22, 2016 · US
US10000439B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10000439-B2 |
| Application number | US-201314650906-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 16, 2013 |
| Priority date | Dec 17, 2012 |
| Publication date | Jun 19, 2018 |
| Grant date | Jun 19, 2018 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The invention relates to the production of alkyl acrylate according to a continuous transesterification process. In one embodiment the process of the invention uses a simple column to purify a reaction mixture of acryl acrylate in one step yielding alkyl acrylate with a purity of greater than 99.8%.
Opening claim text (preview).
The invention claimed is: 1. A process for the continuous production of alkyl acrylates, by a transesterification reaction between a light alkyl acrylate and a heavy alcohol in the presence of at least one catalyst and at least one polymerization inhibitor, said transesterification reaction represented by the reaction: H 2 C═CHCOOR 1 +R 2 OH⇄H 2 C═CHCOOR 2 +R 1 OH wherein R 1 is a methyl or ethyl group, R 2 is a linear or branched alkyl group having 4 to 9 carbon atoms, and optionally comprising a nitrogen atom, carrying out said reaction in a reactor coupled to a distillation column from which an azeotropic mixture comprising light alkyl acrylate and light alcohol generated by the transesterification reaction is drawn off, sending a crude reaction product comprising unreacted reactants, formed reaction products, catalyst(s) and polymerization inhibitor(s) to a single distillation column which is a simple column lacking a vertical divided wall and under reduced pressure for distillation, whereby the distillation yields: at a top portion, a stream of light products consisting essentially of residual alcohols R 2 OH and R 1 OH and unreacted reactant H 2 C═CHCOOR 1 , which is recycled to the reactor, in a bottom portion, product H 2 C═CHCOOR 2 which is drawn off laterally in a gas phase, at a bottom, a stream of heavy reaction products comprising the catalyst(s), the polymerization inhibitor(s) and H 2 C═CHCOOR 2 which is recycled in part to the reactor; such that said process produces said alkyl acrylates have a purity greater than 99.8%. 2. The process as claimed in claim 1 , wherein the single distillation column processing the crude reaction product is a simple column containing distillation plates with or without downcomers, or containing packing of random or structured type, optionally with recentering plates for the distribution of liquid, able to operate at pressures below atmospheric pressure. 3. The process as claimed in claim 1 wherein the alcohol R 2 OH is selected from the group consisting of 2-octanol, 2-ethylhexanol and N,N-dimethylaminoethanol. 4. The process as claimed in claim 3 wherein the alcohol is 2-octanol. 5. The process as claimed in claim 1 wherein the transesterification catalyst is an alkyl titanate of formula Ti(OR 1 ) 4 or Ti(OR 2 ) 4 in solution in the alcohol R 1 OH and/or R 2 OH. 6. The process as claimed in claim 1 wherein R 1 is an ethyl group. 7. The process as claimed in claim 1 wherein the catalyst is present in an amount of 5×10 −4 to 5×10 −2 mol per mole of R 2 OH. 8. The process as claimed in claim 1 wherein compound H 2 C═CHCOOR 1 and the compound R 2 OH have a molar ratio between 1 and 3. 9. The process as claimed in claim 1 wherein the transesterification reaction is carried out at a pressure between 350 mmHg (0.47×10 5 Pa) and atmospheric pressure, and at a temperature between 90° C. and 150° C. 10. The process as claimed in claim 1 for the manufacture of 2-octyl acrylate, using ethyl titanate and/or 2-octyl titanate in 2-octanol as the catalyst.
from hydroxy amines by reactions involving the etherification or esterification of hydroxy groups · CPC title
by distillation · CPC title
by reacting an ester group with a hydroxy group · CPC title
Recycling of unreacted starting or intermediate materials · CPC title
Acrylic acid esters; Methacrylic acid esters · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.