JP2006272205A - Waste treatment device and waste treatment method - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide a waste treatment device for treating a large amount of waste by partially altering an existing cement manufacturing apparatus. <P>SOLUTION: The waste treatment device is obtained by partially altering the cement manufacturing device, which is provided with a preheater 1 having a raw material charge port 9 on the upper part and a rotary kiln 2 connected to the lower part of the preheater 1. The waste treatment device is provided with: a waste supply path 15 for supplying the waste into the rotary kiln 2 on the kiln rear side of the rotary kiln 2; and a recovery path 16 for recovering the reaction product of a neutralizer for waste gas charged from the raw material charge port 9 on the lower part of the preheater 1. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

  The present invention relates to an apparatus and method for treating waste such as municipal waste, incineration ash, incineration fly ash, molten fly ash, biomass, waste plastic, and contaminated soil.

Conventionally, a technique using waste such as incinerated ash has been proposed as a part of clinker raw material in a cement manufacturing apparatus.
For example, supplying a raw material containing heavy metal-containing dust such as garbage incineration ash to a rotary kiln, firing with a burner, and exhausting exhaust gas containing volatile matter (lead chloride, etc.) from the heavy metal-containing dust from the rotary kiln, Cooling with a cooling device to obtain fine dust consisting of heavy metal chlorides (lead chloride, etc.) and exhaust gas containing coarse particle dust, classifying the exhaust gas with a cyclone, and using coarse particle dust as cement raw material A treatment method for heavy metal-containing waste including a step of returning to a rotary kiln and firing while sending fine dust made of heavy metal chloride to a dust collector and collecting it has been proposed (Patent Document 1). .
This technology pays attention to the fact that waste metals such as incineration ash contain heavy metals and chlorine, and after volatilizing heavy metals and chlorine at a high temperature by the chlorination volatilization method, the exhaust gas containing this volatile matter is cooled. By doing so, chlorides of heavy metals are generated as fine dust and collected by a dust collector.
JP 11-239774 A

In the technique described in the above-mentioned document, waste such as incineration ash is used as a part of clinker raw material in a cement manufacturing apparatus. In other words, this technology burns clinker using ordinary clinker raw materials (limestone, clay, silica stone, iron slag, etc.) and wastes such as incineration ash. From the viewpoint of maintaining the quality of clinker, It is necessary to limit the amount of goods used. For this reason, there is a problem in that there is a limit to the quantitative treatment capacity of waste.
On the other hand, in order to adjust the production amount of cement, the operation of the cement manufacturing apparatus may be suspended. Utilizing such an existing cement manufacturing apparatus for other purposes is desirable in terms of effective use of existing facilities. However, the present situation is that it is difficult to divert the cement production apparatus to other uses because the cement production apparatus has a unique structure.
Therefore, the present invention provides a waste processing apparatus that is a means for processing a large amount of waste by partially remodeling an existing cement manufacturing apparatus, and a waste processing method using the apparatus. Objective.

As a result of intensive studies to solve the above-mentioned problems, the present inventor has found that waste for supplying waste such as municipal waste to the kiln bottom side of the rotary kiln with respect to a cement manufacturing apparatus equipped with a preheater and a rotary kiln. While providing a supply path, the raw material input port is used as an input port for the exhaust gas neutralizer (for example, slaked lime), and the reaction product of the exhaust gas neutralizer that moves downward in the preheater (for example, calcium sulfate) , Calcium chloride, etc.), a waste treatment device provided at the lower part of the preheater can process a large amount of waste, and can also be used for aggregate, mine backfill, cement can be obtained fired product can be used in the raw material, further volumes of acid gas components (SO _x, HCl, etc.) contained in the exhaust gas occurring in the rotary kiln Found that can be removed to the collection, the present invention has been completed.

That is, the present invention provides the following [1] to [4].
[1] A waste treatment apparatus obtained by partially modifying a cement manufacturing apparatus including a preheater having a raw material inlet at an upper portion and a rotary kiln connected to the lower portion of the preheater, the kiln bottom side of the rotary kiln In addition, a waste supply path for supplying waste into the rotary kiln is provided, and a reaction of a neutralizer for exhaust gas (for example, slaked lime) supplied from the raw material input port to the lower part of the preheater A waste treatment apparatus comprising a collection path for collecting a product (for example, calcium sulfate, calcium chloride, etc.).
[2] A waste treatment method using the waste treatment apparatus according to [1], wherein (a) a waste supply step of supplying waste into the rotary kiln through the waste supply path; b) a firing step in which the waste is heated in the rotary kiln to generate a fired product and exhaust gas; and (c) a neutralizer for exhaust gas is supplied into the preheater through the raw material inlet, and the preheater An exhaust gas neutralization step of reacting the exhaust gas neutralizer with the exhaust gas to generate a reaction product, and (d) a product recovery step of recovering the reaction product via the recovery path. A waste treatment method comprising:
[3] (e) The above reaction product recovered in step (d) is washed with water and then separated into solid and liquid to obtain a solid and a liquid, and (f) obtained in step (e). The waste treatment method according to the above [2], which comprises using the solid content as a waste in the step (a) or a solid content utilization step as a neutralizer for exhaust gas in the step (c).
[4] The waste treatment method according to [2] or [3], wherein a calcium-based neutralizer is used as the exhaust gas neutralizer.

The waste treatment apparatus of the present invention treats a large amount of waste using an existing cement production apparatus, and the problem of idleness of the cement production apparatus accompanying the adjustment of the production amount of cement and the landfill site This is a solution to the problem of waste disposal, which is becoming difficult to secure, and has extremely high utility value.
In addition, the waste treatment apparatus of the present invention can be completed by performing a slight modification to the existing cement production apparatus, and therefore, the amount of capital investment can be greatly reduced compared to the case of newly establishing a waste treatment plant. be able to.
The waste treatment apparatus of the present invention recovers a reaction product (for example, calcium sulfate, calcium chloride, etc.) of the neutralizer for exhaust gas through a recovery path below the preheater and is included in the exhaust gas. The acidic gas components (SOx, HCl, etc.) that have been removed can be easily removed and recovered.
Furthermore, the fired product obtained by the waste treatment apparatus of the present invention can be used as an aggregate, a mine backfill material, a clinker material, and the like.

Hereinafter, embodiments of the waste treatment apparatus of the present invention will be described with reference to the drawings.
FIG. 1 is a diagram schematically illustrating an example of a waste treatment apparatus according to the present invention, and FIG. 2 is a diagram illustrating a cement manufacturing apparatus before remodeling the waste treatment apparatus illustrated in FIG. In addition, in the figure, each part which has the same name is attached | subjected the same code | symbol.
As shown in FIG. 1, the waste treatment apparatus of the present invention is manufactured by partially modifying the cement manufacturing apparatus shown in FIG.
In FIG. 2, the cement manufacturing apparatus is generally used from the past, and is opposite to the preheater 1 having a raw material inlet at the top, the rotary kiln 2 connected to the bottom of the preheater 1, and the preheater 1. A cooler 3 connected to the end of the rotary kiln on the side (front side of the kiln) is provided.
In the cement manufacturing apparatus, the clinker raw material introduced from the raw material introduction port 9 is preheated in the preheater 1 and decarboxylated, and then enters the rotary kiln 2 from the cyclone 4a which is a constituent part of the preheater 1 through the raw material path 7a. It is supplied and heated at a predetermined temperature in the rotary kiln 2 to become a clinker which is a fired product. The clinker falls on the cooler 3 at the end of the rotary kiln 2 and is collected after being cooled in the cooler 3. The collected clinker is pulverized and then mixed with a predetermined amount of gypsum to become cement.

In contrast to the cement manufacturing apparatus configured as described above, the waste treatment apparatus of the present invention is a waste for supplying waste into the rotary kiln 2 on the kiln bottom side of the rotary kiln 1 as shown in FIG. A supply path 15 is provided, and instead of a raw material path 7a (see FIG. 2) connecting the cyclone 4a and the rotary kiln 2, a recovery path 16 for recovering the solid content in the cyclone 4a without introducing it to the rotary kiln 2 is provided. It is characterized in that it has.
More specifically, the waste treatment apparatus of the present invention includes a preheater 1 having a raw material inlet 9 at the top, a rotary kiln 2 connected to a mixing chamber 5 that is a component of the preheater 1, a mixing chamber 5, A waste supply path 15 provided so as to have an input port between the rotary kiln 2 and a solid component (reaction product of the neutralizing agent for exhaust gas) in the cyclone 4a which is a constituent part of the preheater 1 are collected. A recovery path 16, a treatment means (water tank 17, solid-liquid separator 18, waste water treatment apparatus 19, etc.) of the solid recovered via the recovery path 16, and a cooler connected to the end of the rotary kiln 2 on the front side of the kiln 3 and exhaust gas processing means (gas passage 12, gas cooling tower 13, bag filter 14 and the like) connected to the upper part of the preheater 1.

The preheater 1 includes cyclones 4a to 4d, a mixing chamber 5, a calcining furnace 6, raw material paths 7b to 7e, and gas paths 8a to 8d. Among these, the raw material paths 7b to 7e are paths through which only the solid content can flow, and the gas paths 8a to 8d are paths through which the solid content and exhaust gas can flow.
The raw material inlet 9 uses the clinker raw material inlet (raw material inlet) in the cement manufacturing apparatus as the neutralizer inlet in the waste treatment apparatus of the present invention. For convenience, the name “raw material inlet” is used as it is. Also for the raw material paths 7b to 7e, for convenience of explanation in the present specification, the name of the “raw material path” in the cement manufacturing apparatus is used as it is.
Cooling air for cooling the fired product discharged from the rotary kiln 2 is introduced into the cooler 3. A part of the cooling air passes through the cooler 3, then passes through the gas path 11 in a state of being heated, and is guided to the calcining furnace 6. The remainder of the cooling air is used as combustion air for the burner 10 and then treated as exhaust gas from the rotary kiln 2.
Examples of the waste supply path 15 include a structure in which a screw body is disposed inside a cylindrical casing, and the screw body is rotated to push waste into the rotary kiln 2.

Next, a waste disposal method will be described.
The waste treatment method of the present invention treats waste using the above-described waste treatment apparatus, and (a) a waste supply process for supplying waste into a rotary kiln via a waste supply path; (B) a firing step in which waste is heated in a rotary kiln to produce a fired product and exhaust gas; and (c) an exhaust gas neutralizer is supplied into the preheater via the raw material inlet, and the exhaust gas is exhausted in the preheater. The present invention includes an exhaust gas neutralization step in which a neutralizing agent and exhaust gas are reacted to generate a reaction product, and (d) a product recovery step in which the reaction product is recovered through a recovery path.
In addition to the steps (a) to (d), the waste treatment method of the present invention includes (e) a water washing step in which the recovered reaction product is washed with water and then separated into solid and liquid to obtain a solid and liquid. And (f) a solid content use step in which the obtained solid content is used as a waste in the step (a) or a neutralizer for exhaust gas in the step (c).
Hereinafter, each step will be described.

[Step (a)]
In order to process the waste using the above-described waste processing apparatus, first, the waste is put into the kiln bottom side of the rotary kiln 2 through the waste supply path 15.
Here, the waste which is the object to be treated of the present invention includes municipal waste, incineration ash, incineration fly ash, molten fly ash, waste plastic, biomass, contaminated soil, and the like. Water-containing organic substances such as garbage can also be included in the object to be treated of the present invention by fermentation and drying in advance.
[Step (b)]
The waste supplied into the rotary kiln 2 is heated at a predetermined temperature (for example, 1,100 to 1,400 ° C.) by the burner 10 of the rotary kiln 2 to become a fired product. As the fuel for the burner 10, fossil fuel such as pulverized coal, combustible waste such as waste plastic, and the like are used.
The fired product is recovered after being cooled by the cooler 3, and is used as an aggregate, a mine backfill material, a clinker raw material, etc. after removing chlorine and the like by a water washing treatment as required.
The exhaust gas generated in the rotary kiln 2 passes through the mixing chamber 5, the gas path 8 a, the gas path 8 b, the gas path 8 c, and the gas path 8 d in this order, and then is guided to the gas cooling tower 13 through the gas path 12. In the gas cooling tower 13, a part of volatile matter in the exhaust gas becomes dust. The dust in the exhaust gas that has passed through the gas cooling tower 13 is collected by the bag filter 14. The exhaust gas that has passed through the bag filter 14 is guided to a chimney after passing through another exhaust gas purification device (for example, an active coke tower) as necessary, and is discharged into the atmosphere.

[Step (c)]
A neutralizer for exhaust gas for neutralizing acidic gas components (SO _x , HCl, etc.) in the exhaust gas is input from the raw material input port 9 provided on the side wall of the gas path 8d of the preheater 1. The neutralizing agent for exhaust gas is desirably in the form of fine powder or slurry, for example, in order to promote the neutralization reaction. For example, when the neutralizer for exhaust gas is added in the form of a slurry, the water in the slurry bumps and evaporates in the preheater 1 to generate porous neutralizer particles. The reaction efficiency with the gas component is increased.
A preferable example of the neutralizing agent for exhaust gas includes a Ca-based neutralizing agent. When a Ca-based neutralizing agent is used, a calcium salt is obtained as a reaction product of neutralization. Therefore, after the calcium salt is treated in a subsequent step to form calcium hydroxide, the calcium hydroxide is converted into step (a). By adding to the waste, a fired product that can be used as an aggregate or a clinker raw material can be obtained.
Examples of the Ca-based neutralizer include calcium carbonate (CaCO ₃ ), slaked lime (CaOH), quick lime (CaO), and the like. Calcium carbonate is decarboxylated in the preheater to generate carbon dioxide. Limestone fine powder may be used as calcium carbonate.

The neutralizing agent for exhaust gas (for example, slaked lime) charged from the raw material inlet 9 is the gas path 8d, cyclone 4d, raw material path 7e, gas path 8c, cyclone 4c, raw material path 7d, gas path 8b, cyclone 4b, raw material. In the process of moving in order of the path 7c, the calcining furnace 6, the raw material path 7b, the mixing chamber 5, the gas path 8a, and the cyclone 4a, the reaction product reacts with acidic gas components (SO _x , HCl, etc.) in the exhaust gas. (For example, calcium sulfate, calcium chloride, etc.). A part of the neutralizing agent for exhaust gas may reach the cyclone 4a without being reacted.
The use amount of the neutralizing agent for exhaust gas may be an amount that can sufficiently neutralize the acidic gas component in the exhaust gas. Even when an excess amount of the neutralizing agent for exhaust gas (for example, Ca-based neutralizing agent) is used, the neutralizing agent for exhaust gas recovered unreacted is subjected to a washing step and the like with the sulfuric acid content and It becomes a solid content (for example, calcium hydroxide) that does not contain chlorine, and this solid content may be added to the waste in step (a) or reused as a neutralizing agent for exhaust gas. Absent.
However, since an excessive amount of the neutralizing agent for exhaust gas is disadvantageous in terms of cost, the amount of the neutralizing agent for exhaust gas is preferably used with respect to acidic gas components (SO _x , HCl, etc.) in the exhaust gas. The equivalent is 1 to 10 times, more preferably 2 to 5 times.
[Step (d)]
The reaction product in the cyclone 4a and the unreacted exhaust gas neutralizing agent are recovered through a recovery path 16 connected to the cyclone 4a.

[Step (e)]
The solids (reaction product and exhaust gas neutralizing agent) recovered through the recovery path 16 are put into a water tank 17 with a stirring blade to become a slurry and stirred for a predetermined time, and then a filter press or a belt filter. The solid and liquid are separated by a solid-liquid separation device 18 such as a solid component from which chlorine and sulfuric acid have been removed, and are recovered as a liquid component containing chlorine and sulfuric acid.
In addition, when using Ca type | system | group neutralizing agent as a neutralizing agent for exhaust gas, pH in a water tank is preferably adjusted to 13 or more by adding alkalizing agents, such as sodium hydroxide. If the pH is adjusted within this range, the amount of calcium hydroxide obtained by solid-liquid separation increases, and the calcium recovery rate can be increased.
[Step (f)]
The solid content obtained by solid-liquid separation in the step (e) is made into a fired product that can be used as an aggregate, a mine backfill material, a clinker raw material, etc. in addition to the waste of the step (a), or a raw material It returns to the inlet 9 and is reused as a neutralizing agent for exhaust gas in the step (c).

It is a figure which shows typically an example of the waste disposal apparatus of this invention. It is a figure which shows the cement manufacturing apparatus before converting into the waste disposal apparatus shown in FIG.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Preheater 2 Rotary kiln 3 Cooler 4a, 4b, 4c, 4d Cyclone 5 Mixing chamber 6 Calcining furnace 7a, 7b, 7c, 7d, 7e Raw material path 8a, 8b, 8c, 8d Gas path 9 Raw material inlet 10 Burner 11, 12 Gas path 13 Gas cooling tower 14 Bag filter 15 Waste supply path 16 Recovery path 17 Water tank 18 Solid-liquid separator 19 Waste water treatment apparatus

Claims (4)

A waste treatment apparatus obtained by partially remodeling a cement manufacturing apparatus including a preheater having a raw material inlet at an upper part and a rotary kiln connected to the lower part of the preheater,
A waste supply path for supplying waste into the rotary kiln on the kiln bottom side of the rotary kiln; and
A waste treatment apparatus, comprising a recovery path for recovering a reaction product of a neutralizing agent for exhaust gas input from the raw material input port at a lower portion of the preheater. A waste disposal method using the waste disposal apparatus according to claim 1,
(A) a waste supply step of supplying waste into the rotary kiln via the waste supply path;
(B) a firing step for heating the waste in the rotary kiln to generate a fired product and exhaust gas;
(C) The exhaust gas neutralizer is supplied into the preheater via the raw material inlet, and the exhaust gas neutralizer and the exhaust gas are reacted in the preheater to generate a reaction product. Japanese process,
(D) a waste disposal method comprising a product recovery step of recovering the reaction product via the recovery path. (E) The above-mentioned reaction product recovered in the step (d) is washed with water, followed by solid-liquid separation to obtain a solid content and a liquid content,
The waste according to claim 2, further comprising: (f) the solid content obtained in the step (e) is used as a waste in the step (a) or as a neutralizer for exhaust gas in the step (c). Processing method. The waste treatment method according to claim 2 or 3, wherein a calcium-based neutralizer is used as the exhaust gas neutralizer.

Images