JP2008006355A - Drying method of cement burning apparatus and high-moisture organic waste - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a cement burning apparatus without a possibility of explosion and a deterioration of heat efficiency of a cement kiln when high-moisture organic waste such as high-moisture organic sludge is dried, and to provide a drying method of the high-moisture organic waste. <P>SOLUTION: The cement burning apparatus 1 comprises a dryer 6 supplied with a combustion gas extracted from an exhaust gas flow path from the outlet duct of a calciner 4 of the cement kiln 2 to the outlet duct of a pre-heater 3 to dry the high-moisture organic waste W containing a moisture of 40 mass% or larger. Since the combustion gas extracted from the above-described area has a low oxygen concentration of about 2 to 8%, there is no possibility of explosion. The temperature of the combustion gas is about 450 to 900°C to enable the high-moisture organic waste to be sufficiently dried. A second exhaust gas flow path 8 can be provided to return an exhaust gas from the dryer 6 to the exhaust gas flow path from the outlet duct of the calciner 4 of the cement kiln 2 to the outlet duct of the pre-heater 3. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to a cement baking apparatus capable of safely and efficiently drying high water content organic waste such as high water content organic sludge, and a method for drying high water content organic waste using the same device.

  Conventionally, various apparatuses and methods have been proposed in treating waste such as municipal waste with a cement baking apparatus. For example, in Patent Document 1, a part of the high temperature air of the clinker cooler is introduced into a drying device for drying waste such as municipal waste, and the exhaust from the drying device is returned to the clinker cooler again. A technique of using high-temperature air of a clinker cooler mixed with slag as combustion air for a cement kiln or a calciner is disclosed.

  Moreover, in patent document 2, when incinerating combustible waste with a cement baking apparatus, combustible waste was incinerated using a part of high temperature air of a clinker cooler, and was produced | generated during the incineration process of waste. A technique is described in which exhaust gas is passed through a preheater for heating cement raw material and slag generated during the incineration process of waste is drawn out.

JP 63-151650 A Special table 2003-506299 gazette

  However, as described in the above-mentioned patent document, there is no problem when high-temperature air extracted from the clinker cooler is used for waste such as municipal waste or drying of combustible waste. When the above-mentioned high-temperature air is used for drying a highly water-containing organic waste, such as high-temperature air, the high-temperature air has a high oxygen concentration, which may cause an explosion.

  Moreover, even if it is going to utilize the combustion exhaust gas after the preheater exit of a cement baking apparatus, since the temperature of the combustion exhaust gas of this area | region is about 450 degrees C or less, it is not suitable for drying of a high water content sludge.

  Furthermore, the extraction gas from the kiln bottom of the cement kiln is suitable for drying high water content organic waste because of its low oxygen concentration and high temperature of about 1000 ° C., but when the combustion gas is extracted from the kiln bottom, There was a problem that the thermal efficiency of the cement kiln deteriorated.

  In addition to the above, the dry exhaust gas generated after drying organic sludge and the like contains a considerable amount of odor components, and therefore needs to be exhausted after the deodorization treatment. In order to perform a deodorizing process, it is preferable to make the gas containing an odor component into 800 degreeC or more, and the method of deodorizing by introducing gas into combustion areas, such as a calcining furnace, is common. However, when cement kiln exhaust gas is used for drying organic sludge, etc., the dry exhaust gas has a low oxygen concentration. Therefore, if the dry exhaust gas is treated in the combustion region as described above, the combustion state deteriorates and the thermal efficiency of the cement kiln decreases. Therefore, there was a problem that it was not suitable.

  Therefore, the present invention has been made in view of the above problems in the prior art, and there is no risk of explosion when drying high water content organic waste such as high water content organic sludge, and the thermal efficiency of the cement kiln is improved. It aims at providing the drying method of the cement baking apparatus and high water content organic waste which does not deteriorate.

  In order to achieve the above object, the present invention is a cement firing apparatus, which is supplied with a combustion gas extracted from an exhaust gas passage from an outlet duct of a cement kiln calcining furnace to an outlet duct of a preheater, and is 40% by mass or more. It comprises a drying device for drying high water content organic waste containing water.

  The combustion gas extracted from the exhaust gas flow path from the cement kiln calcining furnace outlet duct to the preheater outlet duct has a low oxygen concentration of 2 to 8%. Since it is 450-900 degreeC, a high water content organic waste can fully be dried. Further, since the combustion gas is not extracted from the kiln bottom of the cement kiln, the thermal efficiency of the cement kiln is not deteriorated.

  The cement baking apparatus may include a second exhaust gas flow path for returning the exhaust gas from the drying apparatus to an exhaust gas flow path from an outlet duct of the calcining furnace of the cement kiln to an outlet duct of the preheater. This eliminates the need for deodorizing the dried exhaust gas having a low oxygen concentration containing an odor component to a combustion region such as a calcining furnace, so that the thermal efficiency of the kiln is not deteriorated.

  In the cement baking apparatus, the high water content organic waste may be high water content organic sludge, and papermaking sludge, sewage sludge, bill pit sludge, food sludge and the like can be dried.

  The present invention also relates to a method for drying a high water content organic waste, wherein a part of the combustion gas is extracted from an exhaust gas passage from an exit duct of a cement kiln calcining furnace to an exit duct of a preheater, A high water content organic waste containing 40% by mass or more of moisture is dried using a part of the burned gas. Thereby, as described above, there is no risk of explosion, and the thermal efficiency of the cement kiln is not deteriorated, so that the high water content organic waste can be dried safely and efficiently.

  In the method of drying the high water content organic waste, the combustion gas after drying the high water content organic waste is returned to the exhaust gas flow path from the cement kiln calcining furnace outlet duct to the preheater outlet duct. Can do. Thereby, as described above, dry exhaust gas having an odor component can be treated without causing deterioration of the thermal efficiency of the kiln.

  In the drying method of the high water content organic waste, the high water content organic waste can be a high water content organic sludge such as papermaking sludge, sewage sludge, bill pit sludge, food sludge and the like.

  As described above, according to the present invention, when drying high water content organic waste such as high water content organic sludge, there is no risk of explosion and the heat efficiency of the cement kiln is not deteriorated. A method for drying waste can be provided.

  FIG. 1 shows an embodiment of a cement baking apparatus according to the present invention. The cement baking apparatus 1 includes a cement kiln 2, a preheater 3, a calcining furnace 4, a drying apparatus 6, a fan 7, and the like. Composed.

  The cement kiln 2, the preheater 3 and the calcining furnace 4 have the same functions as those of a conventional cement calcining apparatus. The cement raw material R supplied to the preheater 3 is preheated by the preheater 3 and calcined by the calcining furnace 4. After that, the cement kiln 2 is fired.

  The drying device 6 is supplied with high water content organic waste (hereinafter referred to as “waste”) W such as high water content organic sludge and extracted from the exhaust gas flow path from the lowermost cyclone 3A to the second cyclone 3B. Combustion gas is supplied, and the waste W is dried. Since this combustion gas has a low oxygen concentration of about 2 to 8%, there is no possibility that the drying device 6 will explode. Moreover, since the temperature of this combustion gas is about 800-900 degreeC, a highly water-containing organic waste can be fully dried. The dried waste W may be processed in the cement baking apparatus 1 or may be processed outside the cement baking apparatus 1.

  The fan 7 is provided to introduce combustion gas from the preheater 3 to the drying device 6, and the exhaust of the fan 7 is returned to the exhaust gas flow path from the lowermost cyclone 3 </ b> A to the second cyclone 3 </ b> B via the circulation duct 8. . Thereby, the deodorizing process of the odor component which the dry exhaust gas generated after drying organic sludge etc. contains is performed.

  In the above embodiment, the combustion gas extracted from the exhaust gas flow path from the lowermost cyclone 3A to the second cyclone 3B is supplied to the drying device 6, but from the second cyclone 3B further upstream of the preheater 3. From the exhaust gas flow path (combustion gas temperature is about 700 to 800 ° C.) to the third cyclone 3C, or from the exhaust gas flow path (combustion gas temperature is about 550 ° C. to 650 ° C.) from the third cyclone 3C to the fourth cyclone 3D The combustion gas can be extracted and supplied to the drying device 6. Also, the dry exhaust gas from the drying device 6 is not limited to returning to the exhaust gas flow path from the lowest cyclone 3A to the second cyclone 3B, and can be returned to the same region as when the combustion gas is extracted. .

It is the schematic which shows the whole structure of one Embodiment of the cement baking apparatus concerning this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Cement baking apparatus 2 Cement kiln 3 Preheater 3A Bottom cyclone 3B 2nd cyclone 3C 3rd cyclone 3D 4th cyclone 4 Calciner 5 Kiln bottom 6 Drying device 7 Fan 8 Circulation duct R Cement raw material W High water content organic waste (High water content organic sludge)

Claims (6)

  A combustion apparatus extracted from the exhaust gas flow path from the outlet duct of the cement kiln calcining furnace to the outlet duct of the preheater is provided with a drying device that dries the high water content organic waste containing 40% by mass or more of moisture. A cement firing device.   The exhaust gas from the said drying apparatus is equipped with the 2nd exhaust gas flow path for returning to the exhaust gas flow path from the exit duct of the calcining furnace of the said cement kiln to the exit duct of a preheater. Cement baking equipment.   3. The cement baking apparatus according to claim 1, wherein the high water content organic waste is high water content organic sludge. A part of the combustion gas is extracted from the exhaust gas flow path from the exit duct of the cement kiln calcining furnace to the exit duct of the preheater,
A method for drying a high water content organic waste, comprising drying a high water content organic waste containing 40% by mass or more of moisture using a part of the extracted combustion gas.   5. The high water content according to claim 4, wherein the gas after drying the high water content organic waste is returned to the exhaust gas flow path from the exit duct of the calcining furnace of the cement kiln to the exit duct of the preheater. How to dry organic waste.   6. The method for drying high water content organic waste according to claim 4, wherein the high water content organic waste is high water content organic sludge.

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