Waste heat power generation system of cement calcination plant
A waste heat power generation system of a cement calcination plant includes: an AQC boiler having an economizer, an evaporator and a superheater; and a PH boiler having a first evaporator and a superheater. The PH boiler, in addition to the evaporator and the superheater, has a second evaporator on a PH exhaust gas exit side, and a returned hot water from a flasher is introduced into the second evaporator via a steam drum. A hot water heated by the second evaporator is introduced into the steam drum, and a steam from the steam drum is introduced into the low-pressure stage of the steam turbine.
1. A waste heat power generation system of a cement calcination plant comprising: an air quenching cooler boiler having an economizer, an evaporator and a superheater; and a preheater boiler having a first evaporator and a superheater, the system being structured so that a part of hot water heated by the economizer of the air quenching cooler boiler is introduced into a low-pressure stage of a steam turbine via a flasher, and another one part of the hot water is superheated by the evaporator and the superheater of the air quenching cooler boiler, and still another one part of the hot water is superheated by the evaporator and the superheater of the preheater boiler, so as to introduce a high-pressure steam into a high-pressure stage of the steam turbine, wherein:
the preheater boiler, in addition to the evaporator and the superheater, has a second evaporator on a preheater exhaust gas exit side, and returned hot water from the flasher is introduced into the second evaporator via a steam drum, and
hot water heated by the second evaporator is introduced into the steam drum, and a steam from the steam drum is introduced into the low-pressure stage of the steam turbine.
2. The waste heat power generation system of a cement calcination plant according to claim 1 , wherein a superheated steam pressure by the superheater of the preheater boiler is 13 atg or higher, and a steam pressure by the second evaporator and the steam drum is 3 atg or lower.