Enichem S.p.a

Polimeri Europa S.p.a.

Montedison S.p.a.

Istituto Guido Donegani

Ministero Dell 'universita'e Della Ricerca Scientifica E Technologica

Other

Farmitalia Carlo Erba

Ministero Dell'universita E Della Ricerca Scientifica E Tecnologica

Versalis S.p.a.

Isagro S.p.a.

Medere Srl

Daniele Bianchi

Rossella Bortolo

Pietro Cesti

Giuliana Franzosi

Aldo Bosetti

Walter Cabri

Marco Ricci

Concetta Compagno

Silvia Galafassi

Roberto Buzzoni

Luigi Balducci

Giuseppe Bellussi

Marilena Gusmeroli

Ezio A Battistel

Daniela Cucchetti

Roberto Tassinari

Paolo Golini

Franco Francalanci

Rino D'Aloisio

Raffaele Ungarelli

Rodolfo Vignola

Sandro Spezia

Chiara Busto

Carla Lazzari

Alberto Cesana

Leonardo Dalloro

Maria Angela Mantegazza

Daniele Delledonne

Paolo Bellandi

Lino Carnelli

Giacomo Fernando Rispoli

Sandra Cobianco

Carlo Pina

Norberto Gatti

Maria Altamura

Anna Maria Romano

Mario Baldassarre

Roberto Bagatin

Francesca Pizza

Sergio Soattini

Giuseppe Gioventu

Chiara Sargiotto

Daniele Moscotti

Cristina Tonini

Raffaele Ferrante

Marco Mannisi

Concetta Maria Compagno

A method for concentrating, in order to favour the subsequent extraction process of intracellular lipids, a cell suspension containing a biomass of oleaginous yeasts fermented in fermentation broth under conditions that allow the intracellular accumulation of lipids, where the biomass contains significant quantities of mucilaginous material. The method includes:

Method for concentrating a cell suspension comprising a mucilaginous biomass of oleaginous yeasts

The present invention concerns an oleaginous yeast variant of the speciescharacterized by higher biomass yields and intra-cellular lipid accumulation useful for the production of bio-fuels higher, in determined conditions, with respect to the wild type strain of the same species. Furthermore, the invention concerns a method through which said oleaginous yeast variant of the specieswas obtained. The invention further concerns the lipid production by means of said variant strain of oleaginous yeast of the species

Oleaginous yeast variant, method for obtaining thereof and use thereof for lipid production

Integrated process for the production of bio-oil from sludge coming from a wastewater purification plant comprising the following steps: (a) sending wastewater to said purification plant obtaining sludge; (b) subjecting the sludge obtained in said step (a) to liquefaction, obtaining a mixture Including an oily phase consisting of bio-oil, a solid phase and an aqueous phase; (c) sending the aqueous phase obtained in said step (b) to said purification plant. The bio-oil (or 'bio-crude') thus obtained can be advantageously used in the production of bio-fuels which can be used as such, or in a mixture with other automotive fuels. Otherwise, said bio-oil (or 'bio-crude') can be used as such (bio-fuel), or in a mixture with fossil fuels (combustible oil, coal, etc.), for the generation of electric energy or heat.

Integrated process for the production of bio-oil from sludge coming from a wastewater purification plant

A process for the conversion of lignin to liquid hydrocarbons comprising:

Process for the conversion of lignin to liquid hydrocarbons

Process for the production of lipids from biomass comprising polysaccharides. The biomass is subjected to acid hydrolysis to obtain a solid phase and an aqueous phase. The solid phase is subjected to acid or to enzymatic hydrolysis obtaining a further solid phase and a further aqueous phase. The aqueous phases obtained from both hydrolysis steps are subjected to fermentation with an oleaginous yeast. The obtained fermentation broth comprises oleaginous cellular biomass which is subjected to microfiltration for the isolation of lipids. Said lipids can be used in the production of biodiesel or green diesel.

Process for the production of lipids from biomass

A process for the production of bio-oil from solid urban waste, comprising the following steps: a) subjecting said solid urban waste to liquefaction, obtaining a mixture including an oily phase consisting of bio-oil, a solid phase and an aqueous phase; b) subjecting the aqueous phase obtained in the liquefaction step a) to fermentation, obtaining a fermented biomass; c) feeding the fermented biomass obtained in the fermentation step b) to the liquefaction step a). The bio-oil (or bio-crude) thus obtained can be advantageously used in the production of biofuels which can be used as such or mixed with other motor vehicle fuels. Alternatively, this bio-oil (or bio-crude) can be used as such (biocombustible) or mixed with fossil combustibles (combustible oil, coal, etc.) for the generation of electric energy or heat.

Process for the production of bio-oil from solid urban waste

A process to activate a titanium silicalite catalyst for the oxidation of benzene to phenol is provided. The catalyst is activated in the reactor for the oxidation by feeding to a reactor containing the titanium silicalite catalyst, during a time of from 2 to 6 hours, at a temperature ranging from 20 to 120&#xb0; C., an aqueous solution of ammonium acid fluoride in a concentration ranging from 0.1% to 1% by weight; and hydrogen peroxide in a concentration ranging from 3% to 10% by weight; feeding water to the reactor at the end of the reaction; and drying or calcining the catalyst contained in the reactor to obtain the activated catalyst. The catalyst is represented by the formula:TiO.(1&#x2212;)SiO

Method to activate a catalyst for a continuous process for the preparation of phenol from benzene in a fixed bed reactor

The cultivation of heterotrophic and phototrophic micro-organisms is integrated for the production of bio-oil for biofuels, wherein the overall algal suspension produced is first thickened, with recirculation of the excess water to cultivation containers, and then thermally treated at a high temperature. After cooling, a bio-oil phase is recovered together with a suspension rich in soluble carbohydrates and proteins which forms a nutritional/energy source for heterotrophic micro-organisms.

Integrated process for the production of bio-oil from micro-organisms

The invention relates to a continuous process for the preparation of phenol by means of the direct oxidation of benzene with hydrogen peroxide in the presence of a catalyst based on titanium silicalite TS-1 comprising: (a) running the process in a fixed bed reactor containing the catalyst based on TS-1 at a temperature ranging from 80-120&#xb0; C. and at a pressure ranging from 3-15 atm; (b) feeding to the reactor a stream containing HO, benzene, sulfolane and water in a single or double phase, wherein the quantities of the single components are within the range of 0.2-6, 15-60, 30-80, 0.5-30 parts by weight, respectively, for every 100 units fed and whose total flow rate is calculated so that the residence time in the reactor (defined as the ratio between the quantity of catalyst by weight and the feeding flow rate) ranges from 0.3 to 2 min; (c) recovery of the products, by-products and solvent from the liquid stream leaving the reactor.

Continuous process for the preparation of phenol from benzene in a fixed bed reactor

The invention relates to a process for the preparation of phenol comprising the following phases:

Integrated process for the preparation of phenol from benzene with recycling of the by-products

Process for the recovery of phenol and biphenols

A method is described for improving the catalytic performances of titanium silicalite having formula (I) by the activation of the catalyst (I) in an aqueous medium with hydrogen peroxide, in the presence of precursors of fluoride ions or anionic species containing fluorine. The activated catalyst (I) is particularly useful in oxidation processes with hydrogen peroxide of organic substrates and, in particular, in hydroxylation reactions of aromatic compounds, amoximation reactions of carbonyl compounds, epoxidation reactions of olefinic compounds and oxidation reactions of nitrogenated compounds.

Activation method of titanium silicalite

The invention relates to a process for the hydroxylation of aromatic hydrocarbons by direct oxidation with hydrogen peroxide. The process is carried out in the presence of a catalyst comprising:

Process for the hydroxylation of aromatic hydrocarbons

An improved process is described for the synthesis of hydroxylated aromatic compounds by means of the oxidation of an aromatic substrate with hydrogen, peroxide in an organic solvent, in the presence of synthetic zeolites, wherein the improvement consists in the fact that the organic solvent is selected from compounds having general formula (I) ##STR1## wherein: R.sub.1, R.sub.2, R.sub.3 and R.sub.4, the same or different, represent a hydrogen atom or an alkyl group with from 1 to 4 carbon atoms or from compounds having general formula (II) ##STR2## wherein R and R', the same or different, represent an alkyl radical with from 1 to 4 carbon atoms.

Process for the oxidation of aromatic compounds to hydroxyaromatic

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Arese, Italy

Daniele Bianchi