Chiyoda Corporation

Junichi Sakaguchi

Osamu Yamamoto

Yoshitsugi Kikkawa

Moritaka Nakamura

Yasuhiro Naito

There is provided a method for producing synthesis gas without COemissions. In the method for producing synthesis gas by reforming a hydrocarbon gas, a reforming reaction is caused by supplying a light hydrocarbon gas containing steam and/or carbon dioxide added thereto to a catalyst-filled tube side of a shell-and-tube heat exchanger-type reformer and circulating a heating medium, such as a molten salt, heated by a heat source such as solar heat or nuclear heat in a shell side of the shell-and-tube heat exchanger-type reformer. Carbon dioxide is removed from a produced gas discharged from the tube side and is supplied to the upstream side of the tube side and recycled.

Non-CO2 emitting manufacturing method for synthesis gas

In a compressor drive system for a natural gas liquefaction plant including a plurality of gas turbines each provided in an individual refrigeration cycle for pressurizing a different refrigerant, an electric motor is provided for each of the gas turbines so as to serve both as an auxiliary electric motor for generating a startup torque and as an AC generator, and the excess output power of the gas turbine is converted into electric power by this electric motor when the power requirement of the associated compressor is less than the power output of the gas turbine. Additionally, at least two of the gas turbines are of an identical make which is suitable for driving the compressor of one of the associated refrigeration cycles requiring a larger driving power. Therefore, the gas turbines can be operated at optimum conditions at all times without regard to seasonal changes of the operating conditions, and the efficient operation of the gas turbines will result in a significant reduction in the operation costs through a substantial saving of fuel consumption. Moreover, any excess power output of one of the gas turbines can be allocated so as to reduce the burden of the in-plant power station and/or to supplement the shortage of the power output of the other gas turbine, and the management of the stand-by units and spare parts can be simplified. These factors have a compounded effect in reducing the investment costs of the plant.

Compressor drive system for a natural gas liquefaction plant having an

Provided is a method for liquefying natural gas which can be readily adapted to LNG plants of all sizes without requiring expensive and special heat exchangers. The liquefaction of feed gas of natural gas and recycle natural gas is carried out with a single-component refrigerant or a mixed refrigerant in a high temperature stage, and with a substantially isentropic expansion in a low temperature stage, and a non-liquefied part of the recycle gas after the expansion step is pressurized with a compressor and recycled along with a recycle stream of non-liquefied par of the feed natural gas, the liquefied part by the refrigerant exchanging heat with the non-liquefied part stream produced from the substantially isentropic expansion, in a plate-fin heat exchanger or the like. The compressor is driven by the power obtained by the substantially isentropic expansion.

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Kanagawa, Japan

Junichi Sakaguchi