61results about How to "Reduce the amount of fly ash" patented technology

A gas-solid separator of a recirculating fluidized bed boiler comprises a downward flue and an upward flue which are separated from front to back by a membrane-type guided flue gas downward and upward turning screen; the downward flue and the upward flue are communicated with each other through a swerving passageway and a feed bin which is hermetically installed below the downward flue and the upward flue; a flue gas inlet is arranged at the front upper part of the gas-solid separator and a flue gas outlet is arranged at the back upper part of the gas-solid separator; four walls of the gas-solid separator are all water cooled walls which are integrated with the boiler; the gas-solid separator further comprises a flow equalizing and separating tube bundle and an abrasion-proof communication pipe which are located on the swerving passageway; the upper end of the flow equalizing and separating tube bundle on the swerving passageway is communicated with a lower cross collecting tank of the membrane-type guided flue gas downward and upward turning screen, and the lower end of the flow equalizing and separating tube bundle on the swerving passageway is communicated with a cross collecting tank of the feed bin; and the upper end of the abrasion-proof communication pipe on the swerving passageway is communicated with the lower cross collecting tank of the membrane-type screen, and the lower end of the abrasion-proof communication pipe on the swerving passageway is communicated with a cross collecting tank of the communication pipe. In the case of circulation at low ratio, inertia gravity is used for single stage separation, and in the case of circulation at high ratio, when the speed of the smoke in the upward flue is high, low-temperature cyclone separation can be combined with inertia gravity separation for double-stage separation.

The invention discloses a gas and solid separator of a recirculating fluidized bed boiler, which comprises a downstream flue and an upstream flue which are partitioned by a guiding flue gas up-down replicating film type screen, wherein the downstream flue and the upstream flue are communicated with storage bins hermetically installed below the downstream flue and the upstream flue through a turning channel, the front upper part of the gas and solid separator is provided with a flue gas inlet, the back upper part of the gas and solid separator is provided with a flue gas outlet, and four walls of the gas and solid separator are all heated water-cooling walls integrated with the boiler; and the gas and solid separator also comprises a uniform flow separating pipe bundle positioned on the turning channel, the upper end of the uniform flow separating pipe bundle on the turning channel is communicated with the guiding flue gas up-down replicating film type screen, and the lower end of the uniform flow separating pipe bundle on the turning channel is communicated with a lower transverse container. The invention also discloses a recirculating fluidized bed boiler containing two sets of gas and solid separators. The recirculating fluidized bed boiler has the advantages of wide application range, advanced process, simple manufacturing and installation, energy saving, consumption reduction and obvious emission reduction.

The invention relates to a sludge drying and incineration combined treatment method with good treatment effect, wide sludge adaptability, and safe and stability system. To avoid agglomeration of mechanically dewatered sludge (k) in a fluidized bed dryer (6), a part of dried sludge (c) is premixed with the mechanically dewatered sludge (k) and then fed into the fluidized bed dryer (6). The dried sludge (c) is incinerated into a circulating fluidized bed incinerator (1) to generate superheated vapor. The superheated vapor is condensed to hot water in a heat exchange tube (6-2) of the fluidized bed dryer (6) and then recycled to the circulating fluidized bed incinerator (1). The arrangement of buried pipes (1-3) and fractional air supply inside the circulating fluidized bed incinerator (1) can effectively control the lower temperature of the circulating fluidized bed incinerator (1) to prevent deflagration of dried sludge. The entire system has no emission of pollutants such as unpleasantodor, acidic gases, heavy metals and dioxin; is safe and reliable; and can operate for a long time.