The present invention relates to a process for manufacturing para-eugenol and/or ortho-eugenol, comprising a step (i) of deallylation of at least one compound of formula (I):

##STR00001##

in which R.sub.1 and R.sub.2 are different, and are chosen from the group consisting of hydrogen and an allyl group (—CH.sub.2—CH═CH.sub.2)

The present invention relates to a process for manufacturing para-eugenol and/or ortho-eugenol, comprising a step (i) of deallylation of at least one compound of formula (I):

##STR00001##

in which R.sub.1 and R.sub.2 are different, and are chosen from the group consisting of hydrogen and an allyl group (—CH.sub.2—CH═CH.sub.2)

The present invention relates to a method for producing a non-rectangular noble metal net (5) on flat bed knitting machines, comprising the steps of providing noble metal wire or noble metal alloy wire providing combustible yarn knitting a net (5) using noble metal wire or noble metal alloy wire for the reaction zone (7), wherein combustible yam is used for the offcut area (9), which is singed off or otherwise removed after the knitting process.

The present invention relates to a method for producing a non-rectangular noble metal net (5) on flat bed knitting machines, comprising the steps of providing noble metal wire or noble metal alloy wire providing combustible yarn knitting a net (5) using noble metal wire or noble metal alloy wire for the reaction zone (7), wherein combustible yam is used for the offcut area (9), which is singed off or otherwise removed after the knitting process.

The present application provides new processes for preparing arachidonoylethanolamine analogues. Intermediates useful for preparing the compounds are also provided.

The present application provides new processes for preparing arachidonoylethanolamine analogues. Intermediates useful for preparing the compounds are also provided.

The present disclosure is directed to an emission treatment system for NO.sub.x abatement in an exhaust stream of an ammonia-fueled engine, the emission treatment system including a selective catalytic reduction (SCR) catalyst disposed on a substrate in fluid communication with the exhaust stream, an oxidation catalyst disposed on a substrate positioned either upstream or downstream of the SCR catalyst and in fluid communication with the exhaust stream and the SCR catalyst, and optionally, one or more adsorption components disposed on a substrate positioned upstream and/or downstream of the SCR catalyst and in fluid communication with the exhaust stream and the SCR catalyst, the adsorption component chosen from low temperature NO.sub.x adsorbers (LT-NA), low temperature ammonia adsorbers (LT-AA), low temperature water vapor adsorbers (LT-WA), and combinations thereof. The disclosure further provides a related method of treatment of an exhaust gas.

The present disclosure is directed to an emission treatment system for NO.sub.x abatement in an exhaust stream of an ammonia-fueled engine, the emission treatment system including a selective catalytic reduction (SCR) catalyst disposed on a substrate in fluid communication with the exhaust stream, an oxidation catalyst disposed on a substrate positioned either upstream or downstream of the SCR catalyst and in fluid communication with the exhaust stream and the SCR catalyst, and optionally, one or more adsorption components disposed on a substrate positioned upstream and/or downstream of the SCR catalyst and in fluid communication with the exhaust stream and the SCR catalyst, the adsorption component chosen from low temperature NO.sub.x adsorbers (LT-NA), low temperature ammonia adsorbers (LT-AA), low temperature water vapor adsorbers (LT-WA), and combinations thereof. The disclosure further provides a related method of treatment of an exhaust gas.

The present disclosure relates to a method for preparation of 1,4-cyclohexanedimethanol. According to the present disclosure, two step reduction reactions are conducted using terephthalic acid as starting material, and an isomerization process for increasing the rate of trans isomers of CHDA is introduced therebetween, thereby providing a method capable of stably preparing CHDM with high rate of trans isomers.

A catalyst device includes a central axis and a catalyst support. The catalyst support includes a slit that is arranged to be orthogonal to the central axis. The slit is arranged to be symmetrical with respect to an arbitrary plane that includes the central axis.