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Pneumatic transport facility for chlorine bypass dust, and cement kiln exhaust gas treatment system equipped with the facility

A pneumatic conveying and waste gas treatment technology, applied in the field of cement kiln waste gas treatment system, can solve problems such as pipeline blockage, water spray nozzle corrosion in the mill, temperature fluctuation at the mill outlet, etc., and achieve the effect of reducing blockage

Inactive Publication Date: 2013-08-21
DENKA CO LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, since the chlorine bypass dust has deliquescence properties, there is a problem that if the wall surface temperature of these storage tanks is lowered, the deliquescence will cause clogging of the pipes, making it difficult to remove the chlorine bypass dust from the storage tanks.
[0013] However, the method of slurrying chlorine bypass dust as described in JP 2000-354838 A is considered to easily cause corrosion and clogging of the water spray nozzles in the mill.
As a result, it is difficult to control the amount of sprayed water from the nozzle, and fluctuations in the amount of sprayed water are likely to cause fluctuations in the temperature at the outlet of the mill, which may also affect fluctuations in cement quality

Method used

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  • Pneumatic transport facility for chlorine bypass dust, and cement kiln exhaust gas treatment system equipped with the facility
  • Pneumatic transport facility for chlorine bypass dust, and cement kiln exhaust gas treatment system equipped with the facility
  • Pneumatic transport facility for chlorine bypass dust, and cement kiln exhaust gas treatment system equipped with the facility

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0067] Make figure 1 The cement kiln exhaust gas treatment system in the embodiment is started for one week under the following operating conditions.

[0068]

[0069] (1) Cement kiln exhaust gas at the inlet of the exhaust pipe 702:

[0070] -Temperature: 900~1100℃,

[0071] -Atmospheric pressure dew point: 60~69℃

[0072] - Air volume: 150[m 3 N / min]

[0073] (2) Air for cooling and dehumidification:

[0074] -External air (temperature: 2 to 16°C, atmospheric dew point: -5 to 11°C)

[0075] - The air volume sent by the blower to the exhaust pipe 702: 250 [m 3 N / min]

[0076] -The air volume sent by the blower to the cooler 705: 320[m 3 N / min]

[0077] (3) The gas flow rate at the outlet of the exhaust pipe 702: 15m / s

[0078] (4) Cement kiln waste gas flowing into inlet 101:

[0079] -Gas temperature: 58~82℃

[0080] -Atmospheric pressure dew point: 30~39℃

[0081] (5) Dust collector 103 of the first dust collection tank 100: bag filter

[0082] (6) Whether t...

Embodiment 2

[0106] In the same manner as in Example 1, except that the operating conditions were changed as follows, figure 1 The cement kiln exhaust gas treatment system in the embodiment started for one week.

[0107]

[0108] (1) Air for cooling and dehumidification:

[0109] -External air (temperature: 2 to 16°C, atmospheric dew point: -5 to 11°C)

[0110] - The air volume sent by the blower to the exhaust pipe 702: 100 [m 3 N / min]

[0111] - The air volume sent by the blower to the cooler 705: 100[m 3 N / min]

[0112] (2) The gas velocity at the outlet of the exhaust pipe 702: 6m / s

[0113] (3) Cement kiln waste gas flowing into inlet 101:

[0114] -Gas temperature: 230~270℃

[0115] -Atmospheric pressure dew point: 43~52℃

[0116] (4) Gas temperature in the pressurized tank 200: 65-98°C

[0117] As a result of starting the cement kiln exhaust gas treatment system under the above operating conditions, there is almost no dust adhesion on the first pipeline 105 , the pressurize...

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Abstract

Provided is a transport facility for chlorine bypass dust, in which the occurrence of a blockage in a pipe can be reduced during the transport of the chlorine bypass dust. A pneumatic transport facility for dust collected from a cement kiln exhaust gas, comprises: a first dust collection tank which is equipped with an inlet port and a discharge port for a cement kiln exhaust gas, a dust collector for collecting dust from the cement kiln exhaust gas, and a discharge port for the collected dust; a pressurized tank which is equipped with an inlet port for the dust from the first dust collection tank, an inlet port for air and an discharge port for pneumatic transport of the dust and which enables the pneumatic transport of the dust by means of compressed air; an air supply source which supplies dried and compressed air having an atmospheric dew point of -35 DEG C or lower to the pressurized tank; and a second dust collection tank which is equipped with an inlet port for dust that is pneumatically transported from the pressurized tank through a second pipe, a dust collector for collecting dust, and a discharge port for air.

Description

technical field [0001] The invention relates to pneumatic conveying equipment for chlorine bypass dust. In addition, the present invention also relates to a cement kiln exhaust gas treatment system equipped with the pneumatic conveying equipment for chlorine bypass dust of the present invention. Background technique [0002] The exhaust gas of cement kiln equipment contains volatile components such as alkaline chloride and alkaline sulfate. These volatile components circulate in the cement kiln equipment between the preheater and the kiln, while gradually concentrating and blending into the clinker, which adversely affects the quality of cement, and also adheres to the preheater, etc. as a coating Therefore, part of the waste gas is extracted from the volatile component concentration area near the kiln tail of the cement kiln (Japanese Patent Application Publication No. 9-175847, Japanese Patent Application Publication No. 11- 35355, Japanese Patent Laid-Open No. 2001-3353...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C04B7/60B01D51/10
CPCF27B7/20F27D17/008
Inventor 西冈朝明柳原靖雄伊藤和之长崎俊一中岛一平渡边晴夫小林稔
Owner DENKA CO LTD