Abstract:
PROBLEM TO BE SOLVED: To provide a method for purifying N-vinylformamide capable of producing high-quality N-vinylformamide for making a polymer having especially high molecular weight having a K value by Fikentscher's method larger than 200. SOLUTION: This N-vinylformamide distillate is obtained by fractional distillation of N-formamide using a column under reduced pressure. The distillation is continuously carried out in the presence of formamide under 0.5-30 millibar measured at the top of the column. The distillation is controlled so that N- vinylformamide having 1-6wt.% formamide content as the distillate is obtained to give the objective N-vinylformamide for producing an N-vinylformamide polymer having a K value larger than 200, containing 1-6wt.% formamide.
Abstract:
PROBLEM TO BE SOLVED: To provide a method for purifying acrylic acid or methacrylic acid, whereby high purity and a high yield of the acid are achieved. SOLUTION: (a) A mixture comprising the acrylic acid or methacrylic acid is subjected to a stringently defined separation treatment essentially in the absence of an organic solvent, this phase is then taken off, (b) at least a part of a residual phase from step (a) is subjected to a less stringently defined separation treatment, and (c) one of phases formed in step (b) is fed to the stringently defined separation treatment in step (a). This method offers a possibility that the overall economical efficiency of the treatment is increased through circulation and that the economical efficiency is improved even when static crystallization is omitted. COPYRIGHT: (C)2007,JPO&INPIT
Abstract:
Způsob frakční kondenzace plynné směsi, která kromě kyseliny akrylové nebo kyseliny metakrylové také obsahuje nejméně jednu další kondenzovatelnou složku a dále vysoký podíl jedné nebo více nekondenzovatelných složek a kde je plynná směs vedena přes kolonu, která má separační vnitřní přepážky a kondenzovatelné složky jsou zkondenzovány chlazením.
Abstract:
Zpusob prípravy kyseliny akrylové nebo kyseliny methakrylové, který zahrnuje: /a/ prípravu smesi plynných produktu, která má slození reakcní smesi z katalytické oxidace alkanu se 3 nebo 4 atomy uhlíku, alkenu se 3 nebo 4 atomy uhlíku, alkanolu se 3 nebo 4 atomy uhlíku a/nebo alkanalu se 3 nebo 4 atomy uhlíku a/nebo jejich prekurzoru, v plynné fáziza vzniku kyseliny akrylové nebo kyseliny methakrylové, pri kterém se provede /b/ kondenzace uvedené smesi plynných produktu, /c/ krystalizace kyseliny akrylové nebo kyseliny methakrylové z roztoku, získaného ve stupni /b/ a /d/ oddelení výsledných krystalu z matecného louhu.
Abstract:
A process for the fractional condensation of a gas mixture which, in addition to acrylic acid or methacrylic acid, also contains at least one further condensable component and additionally a high proportion of one or more noncondensable components, wherein the gas mixture is passed through a column having separatory internals and the condensable components are condensed by cooling.
Abstract:
A process for the fractional condensation of a gas mixture which, in addition to acrylic acid or methacrylic acid, also contains at least one further condensable component and additionally a high proportion of one or more noncondensable components, wherein the gas mixture is passed through a column having separatory internals and the condensable components are condensed by cooling.
Abstract:
Production of partial oxidation products and/or partial ammoxidation products of an olefinic hydrocarbon comprises intermittent operation in a non-operational phase by at least partial non-operation of the dehydration stage whereby the oxidation- and/or ammoxidation zone is continued to be operated and the deficiency in olefinic hydrocarbon feedstock is compensated by another source. A process for the production of partial oxidation products and/or partial ammoxidation products of at least one olefinic hydrocarbon (I) comprises (A) partial dehydration and/or oxy-dehydration of a paraffinic hydrocarbon in a first reaction zone to form a product mixture comprising unreacted paraffinic hydrocarbon and olefinic hydrocarbon (I). (B) separation of the product mixture from (A) into paraffinic and olefinic components optionally in a separation zone and feeding of either the olefinic or paraffinic component to an oxidation and/or ammoxidation zone to form at least one partial oxidation and/or ammoxidation product that contains an olefinic hydrocarbon (I). (C) separation of the product mixture from (B) in a processing zone and recycle of at least a portion of unreacted paraffinic hydrocarbon to the reaction zone of step (A) and (D) from time to time in a non-operational phase at least partial non-operation of the first reaction zone whereby the oxidation- and/or ammoxidation zone (B) is continued to be operated and the deficiency in olefinic hydrocarbon feedstock is at least partially compensated by another source of olefinic hydrocarbon and optionally paraffinic hydrocarbon arising from sources other than reaction zone (A) is at least partially recycled to the oxidation and/or ammoxidation zone (B).