Abstract: A gas supplying system includes a processing gas supply pipe for supplying a processing gas from a gas cylinder 210 into a processing apparatus and a nonreactive gas supply source 230 for supplying a nonreactive gas into the gas supply pipe. While the system is in operation, the gas supply pipe is charged with the nonreactive gas and a control unit is in a standby state. If a processing gas use start signal is received from the processing apparatus, the system exhausts the nonreactive gas from the gas supply pipe to create a vacuum therein; charges the gas supply pipe with the processing gas; and starts a supply of the processing gas from the processing gas supply source. If a processing gas use finish signal is received from the processing apparatus, the system stops the supply of the processing gas from the processing gas supply source; exhausts the processing gas from the gas supply pipe to create a vacuum therein; and charges the gas supply pipe with the nonreactive gas.

Abstract: A gas supplying system includes a processing gas supply pipe for supplying a processing gas from a gas cylinder 210 into a processing apparatus and a nonreactive gas supply source 230 for supplying a nonreactive gas into the gas supply pipe. While the system is in operation, the gas supply pipe is charged with the nonreactive gas and a control unit is in a standby state. If a processing gas use start signal is received from the processing apparatus, the system exhausts the nonreactive gas from the gas supply pipe to create a vacuum therein; charges the gas supply pipe with the processing gas; and starts a supply of the processing gas from the processing gas supply source. If a processing gas use finish signal is received from the processing apparatus, the system stops the supply of the processing gas from the processing gas supply source; exhausts the processing gas from the gas supply pipe to create a vacuum therein; and charges the gas supply pipe with the nonreactive gas.

Abstract: Power consumption of electric equipment used in a semiconductor manufacturing apparatus (100) is obtained and the total amount is displayed as calories by a display means. The semiconductor manufacturing apparatus is configured so that the equipment is set up inside a housing (10). The amount of heat discharged from the inside to the outside (a clean room) via the housing is obtained, and further, the amount of heat removed by exhaust from the interior of the housing and the amount of heat removed by cooling water that cools the equipment is also obtained, and the total amount of heat is displayed. Additionally, factors pertaining to operating costs such as power consumption are measured and their cost obtained, the amount of power consumed is multiplied by a crude oil conversion coefficient to obtain the amount of CO2 generated, and the result is displayed.

Abstract: Power consumption of electric equipment used in a semiconductor manufacturing apparatus (100) is obtained and the total amount is displayed as calories by a display means. The semiconductor manufacturing apparatus is configured so that the equipment is set up inside a housing (10). The amount of heat discharged from the inside to the outside (a clean room) via the housing is obtained, and further, the amount of heat removed by exhaust from the interior of the housing and the amount of heat removed by cooling water that cools the equipment is also obtained, and the total amount of heat is displayed. Additionally, factors pertaining to operating costs such as power consumption are measured and their cost obtained, the amount of power consumed is multiplied by a crude oil conversion coefficient to obtain the amount of CO2 generated, and the result is displayed.

Abstract: An additive for cement comprising a granular molded product formed of a water-reducing agent composed mainly of a naphthalenesulfonic acid/formaldehyde high condensate (NSF) or salt thereof, and a carrier.

Abstract: Slump loss in fresh concrete is prevented by adding a powdery or granular barium, magnesium, iron or aluminum salt of a .beta.-naphthalenesulfonic acid-formaldehyde condensate to the cement or concrete composition. About 0.01 to 10 parts by weight of the condensate per 100 parts by weight of cement, preferably Portland cement, are employed.