Kao Corporation

Yukiko Tabuchi

Takaya Sakai

Hiroko Endo

Masato Nomura

Makiko Shigehisa

Kaoru Ohmae

Kai Yashiro

Provided is a surfactant composition which includes high concentrations of a surfactant, has fluidity in a wide concentration range, and does not become clouded when diluted with hard water. This surfactant composition includes component A, component B, and component C described below, wherein a total content of the component A and the component B is 35 to 80% by mass and wherein the component A is at least one sulfonate compound selected from the group consisting of a hydroxyalkane sulfonate and an olefin sulfonate, the component B is a polyoxyalkylene alkyl ether, and the component C is water.

Surfactant composition

The present invention provides a surfactant composition which includes a surfactant at a high concentration, while having fluidity over a wide concentration range. A surfactant composition according to the present invention contains the components A, B, C and D described below, and is configured such that: the total content of the components A, B and C is from 30% by mass to 80% by mass (inclusive); the mass ratio of the total content of the components A and B to the content of the component C, namely (A+B)/C is from 20/80 to 80/20; and the mass ratio of the content of the component A to the content of the component B, namely A/B is from 98/2 to 45/55. A: an internal olefin sulfonic acid and/or a salt thereof; B: an anionic surfactant other than the component A; C: a nonionic surfactant; D: water.

The present invention relates to a process for producing 2,5-furan dicarboxylic acid by subjecting 5-hydroxymethylfurfural to oxidation reaction in the presence of water, oxygen and an activated carbon-supported metal catalyst containing a noble metal, the process including the following steps (1) and (2) in which the steps (1) and (2) are carried out under a pressure of not less than 0.1 MPa and less than 1.0 MPa while maintaining a reaction solution at a pH of not more than 7, and an amount of the oxygen fed until a time at which the step (2) is terminated is not less than 120 mol % and not more than 140 mol % on the basis of the 5-hydroxymethylfurfural charged: step (1): conducting the oxidation reaction at a temperature of not lower than 50&#xb0; C. and not higher than 110&#xb0; C. until a content of the 5-hydroxymethylfurfural in the reaction solution falls within the range of not less than 0 mg/kg and not more than 1,000 mg/kg; and step (2): subjecting the reaction solution obtained after completion of the step (1) to the oxidation reaction at a temperature of not lower than 140&#xb0; C. and not higher than 250&#xb0; C.

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Izumiotsu, Japan

Yukiko Tabuchi