Oleon Nv

Total Research & Technology Feluy

Pieter Struelens

Julien Deligny

Alys Castel

Nikolai Nesterenko

Jean-Pierre Dath

Delphine Minoux

Sander Van Donk

Pierre Jacobs

Dirk Packet

Cyrielle Huart

Andreas Lambin

Dries Gabriels

Anne-Elise Lescoffit

Enrico Magnabosco

The present invention relates to the use of specific esters in a functional fluid for electric vehicles.

Ester based functional fluid

The present disclosure relates to a composition and a method to use it for releasing the oil trapped in tight oil reservoirs.

Composition comprising polyglycerol-10 fatty acid ester for recovering oil in tight oil reservoirs

The present disclosure relates to a fracturing fluid comprising a specific surfactant combination, its preparation and to a method for releasing the oil trapped in tight oil reservoirs.

Synergetic surfactant combination comprising polyglycerol fatty acid ester and sorbitan ester and/ or ethoxylated sorbitan ester for fracturing fluid

The present invention relates to a composition of branched fatty acids or esters thereof, the process for preparing such a composition and its use in various industrial fields, such as in lubricant, in cosmetics and in home care. More particularly, the present invention relates to a composition comprising at least 30% by weight of polybranched C-Cfatty acids or esters thereof, and a cyclic compound content ranging from 1% to 8% by weight, the weight percentage being given on the total weight of the composition.

Branched fatty acids and esters thereof

A process to make propylene can include providing a reaction zone containing a catalyst and introducing a feedstock into the reaction zone. The catalyst can be an acid. The feedstock can include ethylene, dimethyl ether or methanol and dimethyl ether with at least 1000 wppm of dimethyl ether, and optionally steam. The feedstock can be contacted with the catalyst at temperature and pressure conditions to produce an effluent, including propylene, hydrocarbons, steam, optionally unconverted methanol and/or unconverted dimethyl ether and optionally unconverted ethylene. The temperature at the inlet of the reaction zone can be under 280&#xb0; C., such as from 50 to 280&#xb0; C. The effluent can be sent to a fractionation zone to recover propylene, optionally methanol, dimethyl ether and optionally ethylene. At least a part of methanol, dimethyl ether, and ethylene can be recycled to the reaction zone at step b).

Process to make propylene from ethylene and either dimethyl ether, or methanol and dimethyl ether

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Gooik, Belgium

Pieter Struelens