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Eurotecnica Contractors & Engineers S.p.a.

Eurotecnica Development & Licensing S.p.a.

Sisas Societa Italiana Serie Acetica E Sintetica Spa

Eurotechnica Development & Licensing S.p.a.

Societa Italiana Serie Acetica Sintetica S.p.a.

Sisas S.p.a.

Sisassocieta Italianaserie Acetica Sintetica

Franco Codignola

Antonio Moro

Davino Gelosa

Paolo Gronchi

Elio Santacesaria

Paolo Centola

Roberto Ruggieri

Massimo Morbidelli

Sergio Carra'

Sergio Carra

Andrea Sliepcevich

Giorgio Vergini

Renato Del Rosso

Lucio DiFiore

A poly-&#x3b2;-carboxyacrylamide polymer of formula (I) wherein X is an alkaline metal or a substituent capable of bringing about an exchange reaction with a salt of an alkaline earth metal, said polymer having a ponderal average molecular weight greater than or equal to 2,000. The use of said polymer and process for preparing the same 

Poly-&#x3b2;-carboxyacrylamide polymer, use thereof and process for preparing the same

This invention refers to a process for the synthesis of cumene hydroperoxide and to the product thus obtained. More in particular, this invention refers to a process for the production of cumene hydroperoxide by oxidating cumene with oxygen, where this process is run in the presence of a basic medium insoluble in the reaction environment, and such as not to release inorganic cations to the reaction environment. Such a basic medium is preferably a pyridinic resin. The cumene hydroperoxide thus obtained, characterized by the fact of being free of inorganic cations, is a further object of the invention.

Process for the synthesis of cumene hydroperoxide

Compounds are described, having the following general formula (A) R(CONH&#x2014;CHR0H)(A) and their use as monomers in polymerization and polycondensation reactions.

Aromatic glycols and polyols, preparation process and their use as monomers

This invention refers to a process for the synthesis of phenol and acetone starting from cumene hydroperoxide, and to a plant specifically developed for performing this process. More in particular, this invention refers to a process for the synthesis of phenol and acetone starting from cumene hydroperoxide, comprising the following steps: a) Pretreating of the starting cumene hydroperoxide with acidic resins, to obtain cumene hydroperoxide free of inorganic cations; b) Decomposing of the cumene hydroperoxide free of inorganic cations originating from the step (a) in the presence of acidic resins, to yield phenol and acetone.

Process for the synthesis of phenol and acetone

A novel process for the purification of crude aromatic carboxylic acids, such as, for example, terephthalic acid, orthophthalic acid, trimesic acid, isophthalic acid, 2,6-naphthalenedicarboxylic acid and pyromellitic acid, which are obtained by oxidising the corresponding aromatic precursors is described; the process is based on the subsequent oxidation in heterogeneous phase of the crude product in aqueous solution.

Process for the purification of aromatic carboxylic acids

A description is given here of a novel process for the production of monocarboxylic and polycarboxylic aromatic acids by the catalytic oxidation in homogeneous phase of aromatic compounds carrying at least one oxidizable substituent group attached directly to the carbon atom of the corresponding aromatic nucleus. The novel process according to the present invention comprises the steps of: a) catalytically oxidizing the corresponding aromatic precursors in liquid phase in the presence of gaseous oxygen; b) filtering the end product; c) recycling into the oxidation reactor at least part of the mother liquors resulting from the filtration stage, and is characterized by the fact that said steps from (a) to (c) are carried out in a closed and continuous cycle operating substantially under the same pressure and temperature conditions, preferably at 2-10 barg and 100-140&deg; C.

Apparatus for the production of aromatic acids

Process for producing mono- and poly-carboxylic aromatic acids wherein an aromatic compound having at least one oxidizable substituent directly linked to the carbon atom of the corresponding aromatic nucleus is oxidized in the presence of a catalyst system in the liquid homogenous phase. The oxidation reaction is carried out in aqueous acetic acid, and the catalyst system consists of a combination of cobalt and zirconium organic salts. The oxidation reaction is carried out at an absolute pressure lower than 10 bar and at a temperature of 90-150&deg; C.

Process for the production of aromatic acids

A description is given here of a novel process for the production of monocarboxylic and polycarboxylic aromatic acids by the catalytic oxidation in homogeneous phase of aromatic compounds carrying at least one oxidizable substituent group attached directly to the carbon atom of the corresponding aromatic nucleus. The process comprises a purification step in which the crude product resulting from the oxidation stage is supplied to a filling column containing a bed of material having a high adsorbent power with respect to hafnium and/or zirconium polyoxides, operating at a temperature of from 200 to 300&deg; C. and at a pressure of from 30 to 90 barg.

Process for the production and purification of aromatic acids

An oligomer of an aspartic acid is provided having repeating monomeric units of aspartic acid of the formula: ##STR1## and by a first chain unit having formula: ##STR2## and a chain stopper unit A which is: ##STR3## wherein X is an alkali metal, R represents H or an alkyl containing from 1 to 4 carbon atoms and R.sub.1 is H or the group --COOX.

Polymers of aspartic acid with sequestering activity process for their

There is provided a process for the separation of aromatic hydrocarbons mixtures into single components, in which the mixtures in vapor phase pass onto an adsorption bed formed by a potassium-exchanged Y zeolite, which is preventively saturated with desorbent vapors. According to the invention the desorbent used is isopropylbenzene in vapor phase. This facilitates the quick separation of the pure components, with the exception of the presence of desorbent. The process according to this invention is quicker in comparison to traditional ones. It requires the use of lower charges of desorbent and allows the separation of single pure components of the mixtures. It especially improves the paraxylene separation in higher concentrations with respect to the desorbent.

Process for the separation of mixtures of aromatic hydrocarbons into

The invention relates to a process for the oxidation of unsaturated hydrocarbons, particularly butenes and isobutylene, for the production of acetic acid, propionic acid and acetone. Specifically the invention comprises the highly selective oxidation of an unsaturated hydrocarbon or of a mixture of unsaturated hydrocarbons in the presence of a catalyst consisting of a complex of trivalent cobalt and of a carbonyl compound, of the aldehydic or ketonic type.

Process for the oxidation of unsaturated aliphatic hydrocarbons

A process for the separation of metaxylene from aromatic C.sub.8 hydrocarbons, particularly from ethylbenzene and paraxylene, wherein a first phase is provided in which the mixture of aromatic hydrocarbons is selectively adsorbed, in vapor phase, into a catalytic bed consisting of zeolite of the Y type, preliminarily exchanged with potassium, and in a second phase a desorption is effected with a suitable solvent. The process, carried out at a temperature of 150.degree. to 200.degree. C. and preferably at atmospherical pressure, permits the recovery of metaxylene, substantially pure and at a concentration much higher than that of the starting mixture.

Process for the separation of metaxylene from mixtures of aromatic

The process for the preparation of 1,4-butynediol through the reaction of acetylene with formaldehyde in the presence of a catalytic metal, preferably copper, is improved by using, as the support of the catalytic metal, a molecular sieve or synthetic zeolite to which the catalytic metal is chemically bonded through an ion exchange reaction. There are obtained increased production rates and selectivity and the polymer of acetylene, namely cuprene, is essentially prevented from being formed.

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Milan, Italy

Franco Codignola