Kureha Kagaku Kogyo Kabushiki Kaisha

Hitachi, Ltd.

Tsutomu Konno

Takuji Hosoi

Shinichiro Saito

Kiro Asano

Tadaaki Kato

Yukuo Katayama

Takamasa Arai

Kazuaki Matsui

A data collection server that collects and converts data has a data processor that executes shaping processes to shape collected data, sets a data processing flow based on the shaping processes, sets information of an execution environment of the shaping processes and converts the processing flow based on the information of the execution environment. The processor accepts setting inputs of first and second flags before and after the plurality of shaping processes and performs an integrated shaping process for collectively executing the plurality of shaping processes between the first and second flags when set. The processor also updates information of the execution environment based on execution contents of the integrated shaping process.

Data collection server and data collection method

Dietary fiber, obtained from extracting wheat bran with water, having an average molecular weight of 5.times.10.sup.2 to 1.times.10.sup.5, from 95.3 to 99.0% by weight of a sugar, primarily glucose, and 0.1 to 3.0% by weight protein components. The fiber, when eaten, promotes the digestion and absorption of nutrients, waste excretion and proliferation of Lactobacillus bifidus in the large intestine.

Dietary fiber extracted from wheat bran pharmaceutical and dietary

A process for producing a low sulfur content fuel oil in a high yield from a starting oil having a high sulfur content, which comprises (1) treating a residual petroleum oil with hydrogen at a temperature of about 350.degree. to 450.degree. C and a pressure of about 50 to 200 Kg/cm.sup.2 at a liquid hourly space velocity of about 0.2 to 4 l/H.l in the presence of a catalyst, (2) introducing an inert gas or steam at a temperature of about 400.degree. to 900.degree.C and pyrolyzing the treated oil at a temperature of about 350.degree. to 500.degree.C and at a pressure of about atmospheric pressure to 100 Kg/cm.sup.2 with a residence time of about 0.5 to 10 hours, and (3) hydrodesulfurizing the pyrolyzed oil at a temperature of about 300.degree. to 400.degree.C and a pressure of about 30 to 100 Kg/cm.sup.2 at a liquid hourly space velocity of about 0.5 to 4 l/H.l in the presence of a desulfurizing catalyst.

Process for producing low sulfur content fuel oils

Growing community of inventors

Tokyo, Japan

Tsutomu Konno