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    • 1. 发明专利
    • GENERATION
    • JPH06178598A
    • 1994-06-24
    • JP32935192
    • 1992-12-09
    • MITSUBISHI HEAVY IND LTD
    • MIZOGUCHI AKIYOSHIINOUE YUBUNIIJIMA MASAKIIKUTA YOSHIAKINAKAJIMA MICHIOSHIBATA MASATOSHI
    • C10G7/00C10G32/02F01K23/10F02C3/24F02C7/22H02P9/04
    • PURPOSE:To pick as much fuel as possible that is suitable for a gas turbine from low-sulfur crude oil at low cost and to generate with good heat efficiency by a method wherein gas, whose main ingredient is methane, is simply topped and the obtained low-boiling point fraction is supplied at high temperature to the gas turbine as fuel. CONSTITUTION:Prior to sending low-sulfur crude oil from a crude oil tank 4 to a demineralization process 5, the crude oil is heated in an exhaust heat recovery boiler 2. The demineralized low-sulfur crude oil is supplied to a first simplified topper 6 and the column top gas, together with column top gas of a second simplified topper 8, is gas-liquid separated in a condensation drum 11. Part of it is supplied by a circulating blower 12 to a column bottom of the simplified topper 8 as gas for stripping and the rest is compressed by a gas compresser 13 and is supplied to a gas turbine 1. A condensed fraction in the condensation drum 11 becomes part of fuel for a gas turbine. Out of an intermediate fraction obtained from the column side of the first simplified topper 6, a low boiling point fraction is flown back to the first simplified topper 6 by a first stripper 7 and the rest is used as fuel for a gas turbine.
    • 2. 发明专利
    • GAS TURBINE FUEL
    • JPH06172762A
    • 1994-06-21
    • JP32935292
    • 1992-12-09
    • MITSUBISHI HEAVY IND LTD
    • MIZOGUCHI AKIYOSHIINOUE YUBUNIIJIMA MASAKINAKAJIMA MICHIOSHIBATA MASATOSHI
    • C10L1/04F01K23/10F02C3/24F02C7/22
    • PURPOSE:To obtain a gas turbine fuel by mixing a desalted crude oil or low- sulfur crude oil with a liq. petroleum fuel having V and S contents lower than those of the crude oil to thereby adjust those contents of the crude oil to specified values. CONSTITUTION:A crude oil from a crude oil tank 4 is fed to a waste heat boiler 2, where it is heated to 80-150 deg.C. The oil is then mixed with a preheated plain water at desalters 6 and desalted electrostatically. The desalted oil still at a high temp. is sent to a mixer 7 and mixed with a liq. petroleum fuel, e.g. naphtha, from a liq. petroleum fuel tank 8 in a specified ratio to give a liq. fuel having a V content of 0.5ppm or lower and an S content of 1.3wt.% or lower, which is fed to a gas turbine 1. Power is generated with a generator and a high-temp. exhaust combustion gas is supplied to a waste heat boiler 2. Waste heat is used for generating power with a steam turbine 9, and steam is condensed at a condenser 10 and recirculated to the waste heat boiler 2. The combination of desalting with power generation with the gas turbine 1 enables the effective utilization of a low-grade heat energy and the improvement in power generation efficiency.
    • 3. 发明专利
    • FULL FIRED HEAT RECOVERY THERMAL ELECTRIC POWER GENERATING EQUIPMENT
    • JPH11270355A
    • 1999-10-05
    • JP7153798
    • 1998-03-20
    • MITSUBISHI HEAVY IND LTD
    • KANBARA MASAMICHIOTA KAZUHIROIIJIMA MASAKISHIBATA MASATOSHI
    • F02C7/22C10G9/00F23C6/04
    • PROBLEM TO BE SOLVED: To improve the power generating efficiency while obtaining various fuel with a supply of the only heavy fuel oil and while operating an equipment as a combined electric power generating equipment by providing a heavy fuel oil decomposing unit, a gas turbine, and a boiler for receiving the exhaust gas from the gas turbine and while burning the heavy oil as a fuel. SOLUTION: This power generating equipment includes a heavy fuel oil decomposing unit including a heavy fuel oil heating and decomposing device 1, a gas turbine 2 and a boiler 3 as main equipment. The heavy fuel oil is heated for decomposition by the heavy fuel oil heating and decomposing device 1 so as to obtain the decomposed material including three components of heavy oil, light oil and light gas. The gas turbine 2 rotates a turbine while burning the light oil from the heavy fuel oil decomposing unit. Since oxygen is left in the exhaust gas from the gas turbine 2, the left oxygen is fed to the boiler 3 so as to be used as the combustion air with the recovery of the waste heat. The boiler 3 burns the heavy fuel oil, the heavy oil or the heavy fuel oil from the heavy fuel oil decomposing unit and the heavy oil from the heavy fuel oil decomposing unit as a fuel. The light gas can operate the heavy fuel oil decomposing device 1.
    • 6. 发明专利
    • THERMAL ELECTRIC POWER PLANT
    • JPH11270354A
    • 1999-10-05
    • JP7153698
    • 1998-03-20
    • MITSUBISHI HEAVY IND LTD
    • KANBARA MASAMICHINISHIMURA ISAOMOMOTAKE CHIKANORISHIBATA MASATOSHI
    • F02C7/22C10G7/06C10G9/40F23C6/04
    • PROBLEM TO BE SOLVED: To improve the power generating efficiency while effectively utilizing the high-temperature exhaust gas to be generated in a heavy fuel oil heating and decomposing device or a raw oil heating and fractional distillation device by providing a route for feeding the exhaust gas generated by the combustion of the light gas from a heavy fuel oil decomposing unit in a heavy fuel oil heating and decomposing device to a boiler. SOLUTION: A heavy fuel oil decomposing unit (raw oil fractional distillation unit) including a heavy fuel oil heating and decomposing device (raw oil heating and fractional distillation device) 1, a gas turbine 2 and a boiler 3 are included as main equipment. Especially, a line 20 for feeding the exhaust gas to be generated by combustion of the light gas from the raw oil fractional distillation unit in the raw oil heating and fractional distillation device 1 to a boiler 3 is provided. Heat recovery in the boiler 3 is aimed at by this line 20. The exhaust gas from the raw oil heating and fractional distillation device 1 maintains the predetermined temperature, and efficiency can be remarkably raised by recovering the heat. Furthermore, since a desulfurizer and an NOx removal system in the downstream of the boiler 3 can be utilized, necessity of providing other desulfurizer and NOx removal system dedicated to the raw oil heating and fractional distillation device 1 is eliminated.