KR20070055305A - Retreat method of organic or inorganic waste resources - Google Patents

Abstract

The present invention is the organic and inorganic waste resources of the organic and inorganic waste resources to evaporate the moisture contained in the organic and inorganic waste resources to remove the odor through the reaction heat generated by the simultaneous input of sulfate compound and strong alkali-based powder Provide a reprocessing method.

This not only saves time and costs due to process shortening, but also makes it widely applicable to various organic and inorganic waste resources such as sewage sludge, food waste, livestock waste, waste gypsum, waste lime and dredged soil. In addition, sulphate compounds and strong alkaline powders generated as by-products of industrial processes can use wastes, which are very effective for resource utilization and can effectively remove odors from organic and inorganic waste resources when maintaining proper pH.

Organic and inorganic waste resources, deodorization, simultaneous injection, heat of reaction, sulfate, strong alkali

Description

Reprocessing of organic and inorganic waste resources {RETREAT METHOD OF ORGANIC OR INORGANIC WASTE RESOURCES}

1a to d are photographs showing the reprocessing process of sewage sludge according to the present invention.

2a to d are photographs showing the reprocessing process of purified water sludge according to the present invention.

3a to b are photographs showing the reprocessing process of food waste according to the present invention.

The present invention relates to a method for reprocessing organic / inorganic waste resources, and more particularly, through the heat of reaction generated by simultaneously injecting sulfate compounds and strong alkali powders into the organic / inorganic waste resources. The present invention relates to a reprocessing method for evaporating moisture contained in a resource and removing odors.

Organic and inorganic waste resources can be classified into sewage sludge, purified water sludge, livestock sludge (animal sludge, manure), food waste, waste gypsum, waste lime and dredged soil.

Firstly, sewage and water purification sludge produced in Korea generate more than 3,000 tons of sludge per day from sewage treatment plants, industrial complexes, and end plants, and each single plant or industrial complex. However, there are many problems that occur when reclaiming sludge that contains about 80% of the water, and there are many problems in reclaiming the landfill. It is being tried. In addition, the sludge contains organic materials, so if used properly, energy can be recovered, but when it is disposed of, it can be a source of secondary pollution such as odor generation, and it is desirable to be recycled as resources in terms of waste of effective resources Do.

Waste lime is a concept that collectively refers to limestone residues generated in the process of producing quicklime, slaked lime, carbonate lime, soda ash, etc. by physically and chemically treating limestone, white rock, shell, etc. The waste lime is an environmental pollutant Currently, the landfill is treated in the same way as landfilling, but landfilling is not preferable in terms of resource recycling. Accordingly, various attempts have been made to recycle waste lime. For example, although it was designated for use as a cover material for landfill waste landfill facilities in co-watershed landfills, there was a problem that not only there was a lot of moisture but also a lot of odor was generated, and the development of calcite fertilizer using waste lime was more competitive than investment. It was not commercialized because of low logistics costs due to low and seasonal characteristics. Meanwhile, although sidewalk blocks and bricks have been developed using waste lime, production has not been achieved due to the failure to meet the KS standard and the reduced recycling rate of waste lime. Attempts have been made to develop waste lime as a cement raw material and additive, but this has not been realized due to problems such as facility investment costs.

Waste gypsum is produced in large quantities in the process of desulfurization and in the process of manufacturing phosphoric acid, hydrofluoric acid, boron, and titanium. The gypsum produced in this way contains harmful impurities in itself, which can be used directly for products such as cement and gypsum board. In addition to lowering, there was a limit in throughput. In addition, there is a problem that the risk of groundwater contamination is increased if it is deposited in nature. Furthermore, to date, the waste gypsum can be recycled only through a complex purification process such as washing, neutralizing, calcining, and granulation.

Dredged soil is an inorganic waste resource generated at construction sites, and since 20 to 55% of moisture, 40 to 60% of ash, and 5 to 20% of flammable ash are incinerated, many heat sources are needed. It has been pointed out as the cause.

However, since the waste management law was amended, from July 1, 2003, incineration such as sewage sludge or dumping in the ocean was prohibited. Therefore, the reprocessing of organic and inorganic waste resources became a very important social issue.

On the other hand, in order to recycle the organic-inorganic waste resources without being landfilled, it is necessary to go through a process of solidifying them while reducing the moisture content of the organic-inorganic waste resources having high water content. To this end, conventionally, the chemical treatment before dehydration, but the secondary environmental pollution problem may occur due to the drug has been required to study the physical treatment method before dehydration. Accordingly, a method of maximizing dehydration using ultrasonic waves, which is widely used in the environmental field, has been proposed as a method of treating sludge of high function. This ultrasonic method uses the principle of applying ultrasonic waves to the sludge to break and separate the bonds between the internal and the combined water which are difficult to remove in the sludge by ultrasonic energy.

On the other hand, the solidification treatment method is an engineering method after adding a solidifying agent to dewatered sludge having a high water content. This is by adding a solidifying agent to dewatered sludge to improve the physical and chemical properties of the sludge, thereby promoting work efficiency, harmlessness and stabilization of harmful substances such as heavy metals, and at the same time improving soil mechanical properties such as strength. As the solidifying agent, various cements such as portland cement, crude steel cement, solidified cement, aluminum-based special cement, asphalt, plastic, quicklime, and the like are used.

As an example of manufacturing a solidifying agent used in the solidification treatment method, Korean Patent Application No. 2004-61295 proposes a method of preparing a solidifying agent for sewage sludge treatment by mixing the waste from the workplace with ferrous sulfate crushed powder and strong alkaline powder. It became. The method is effective in recycling the ferrous sulfate, which is a waste, but a solidifying agent is prepared through crushing, mixing, heat dissipation, secondary grinding and secondary mixing, and adding the prepared solidifying agent to sewage sludge. It had to go through a complicated process of solidifying sewage sludge. This method is not only a problem of difficulty in process control and excessive production cost due to multiple processes, but also if the prepared solidifying agent does not create an appropriate environment in the silo before adding to the sewage sludge. Occasionally there was a need for the silo to solidify within the silo and to dispose of the silo. In addition, the method has limitations in application to inorganic waste resources.

Accordingly, the present inventors have made various efforts to overcome the above problems. As a result, the present inventors have made the organic / inorganic composition through reaction heat generated by simultaneously supplying a sulfate compound and a strong alkali powder to an organic / inorganic waste resource without producing a solidifying agent. We have developed a method for reprocessing organic and inorganic waste resources to evaporate moisture and remove odors contained in waste resources.

An object of the present invention is to evaporate the water contained in the organic and inorganic waste resources through the reaction heat generated by the simultaneous input of sulfate compound and strong alkali powder to the organic and inorganic waste resources, and each input and organic and inorganic waste resources It is to provide a method for reprocessing organic and inorganic waste resources to remove odors through chemical reaction.

It is another object of the present invention to provide a method of using organic / inorganic waste resources treated by the reprocessing method for landfill cover and loam soil.

In order to achieve the above technical problem of the present invention, the present invention provides a method for reprocessing an organic / inorganic waste resource, wherein the organic / inorganic waste which simultaneously injects a sulfate compound and a strong alkaline powder into the organic / inorganic waste resource. Provides a way to reprocess resources.

The organic and inorganic waste resources are preferably any one selected from the group consisting of sewage sludge, purified water sludge, food waste, livestock waste, waste gypsum, waste lime and dredged soil.

In the above ratio, preferably, 20 to 35 parts by weight of the sulfate compound and 10 to 15 parts by weight of the strong alkali powder are added to 100 parts by weight of the organic / inorganic waste resource, and more preferably, the sulfate compound and the strong alkali system to be introduced. The powder is preferably maintained at a weight ratio of 6: 4-7: 3 to proceed the process at pH 6-8.

The sulfate compound is preferably calcium sulfate (CaSO ₄ ), potassium sulfate (K ₂ SO ₄ ), sodium sulfate (Na ₂ SO ₄ ), ferrous sulfate (FeSO ₄ ), ferric sulfate (Fe ₂ (SO ₄ ) ₃ ) and Any one or more selected from the group consisting of the hydrates are used.

The strong alkali-based powder is preferably at least one selected from the group consisting of calcium oxide, magnesium oxide, quicklime, slaked lime, limestone and cement.

The present invention provides a landfill material containing organic and inorganic waste resources reprocessed by the above-described method, or provides a landfill soil and a landfill agent.

Hereinafter, the present invention will be described in more detail.

The present invention provides a method for reprocessing an organic / inorganic waste resource by simultaneously introducing a strong acid sulfate compound and a strong alkaline powder into the organic / inorganic waste resource. do.

As described above, a method of reprocessing an organic / inorganic waste resource by reacting a sulfate compound with a strong alkaline material first prepares a solidifying agent through the reaction, and then applies the solidifying agent to the organic / inorganic waste resource. After solidification, it was used as raw materials such as cover material, mature soil, and compost according to the type and purpose of organic waste.

However, this conventional method not only undergoes various steps such as crushing, mixing, heat dissipation, secondary grinding and secondary mixing, but also prepares a separate solidifying agent and reacts it with organic and inorganic waste resources. There were a lot of difficulties. In addition, through the heat dissipation step, there is a waste of energy that can be usefully used, and as a result, the cost increases, thereby raising the reprocessing cost of organic and inorganic waste resources, thereby preventing the vicious cycle of reprocessing the organic and inorganic waste resources. Caused. In addition, when applying the solidifying agent to the organic and inorganic waste resources on the silo, it is often the case that the organic and inorganic waste resources solidify quickly and strongly to discard the entire silo.

On the contrary, the present invention does not produce a solidifying agent as in the conventional method, but simultaneously inputs sulfate compound and strong alkali powder to organic and inorganic waste resources, and the moisture contained in organic and inorganic waste resources through reaction heat generated at this time. It evaporates to solidify organic and inorganic waste resources through chemical reaction between inputs and organic and inorganic waste resources. In addition, the pH is adjusted to 6 ~ 8 to effectively suppress the generation of ammonia to remove odors.

Looking at the reaction mechanism of the present invention in detail as shown in Scheme 1.

MSO ₄ + CaO + H ₂ O (ℓ) ⇒ MO + CaSO ₄ 2H ₂ O + H ₂ O (g) + _Δ H

However, in the above, M is a substance capable of performing acid-alkali exchange reaction by reacting with strong alkali such as Ca, K _{2 ,} Na _{2 ,} Fe, CaO is an exemplary strong alkali substance, and H ₂ O (ℓ) Means moisture contained in inorganic waste resources.

As can be seen in the reaction scheme 1, the reactor operation of the present invention is the SO ₄ of the sulfate when the sulphate and strong alkali powder at the same time to the organic and inorganic waste resources at the same time It absorbs moisture contained in organic and inorganic waste resources at the rate of 160g / kg. Thereafter, stability is found by acid alkali reaction, and the remaining heat in the organic and inorganic waste resources is evaporated through the reaction heat generated at this time. On the other hand, the heat of reaction is different depending on the reaction conditions, but generates approximately 220 ~ 250 ㎉ / mol.

The remaining excess sulfate also reacts with ammonia, the source of malodor, to form the ammonium salt to remove the malodor. To this end, the pH of the acid alkali reaction should be adjusted to 6-8 by appropriately adding the amount of sulfate and strong alkali powder to be added.

The organic and inorganic waste resources are preferably any one selected from the group consisting of sewage sludge, purified water sludge, food waste, livestock waste, waste gypsum, waste lime and dredged soil. In addition, depending on the type and purpose of the organic and inorganic waste resources introduced in the present invention can be effectively utilized in various fields, such as cover material, compost.

In the present invention, the input ratio is preferably 20 to 35 parts by weight of sulfate compound and 10 to 15 parts by weight of strong alkali powder based on 100 parts by weight of organic / inorganic waste resources.

More preferably, the added sulphate compound and the strongly alkaline powder are preferably added at a weight ratio of 6: 4 to 7: 3, and it is advantageous to maintain a pH of 6 to 8.

The reaction conditions of the present invention by the input ratio is preferably carried out at pH 6 ~ 8. The pH range is a very important reaction condition for removing odors of organic and inorganic waste resources. If the reaction proceeds below pH 6, the use of cover material is inappropriate due to low pH, and the reaction exceeds pH 8. If this happens there is a problem difficult to remove odor.

The sulfate compound of the present invention is not limited to the type and size of particle size as long as it can generate heat of reaction through strong alkali powder and acid group reaction, preferably calcium sulfate (CaSO ₄ ), potassium sulfate (K ₂ SO ₄ ), Any one or more selected from the group consisting of sodium sulfate (Na ₂ SO ₄ ), ferrous sulfate (FeSO ₄ ), ferric sulfate (Fe ₂ (SO ₄ ) ₃ ) and hydrates thereof, and sulfuric acid which is a kind of waste The use of ferrous iron is more desirable in terms of resource recycling and cost savings.

The strong alkali-based powder of the present invention is not limited to the type and size of the particle size as long as it can generate the heat of reaction through the acidic reaction with a sulfate compound having a strong acidity, preferably calcium oxide, magnesium oxide, quicklime, calcareous lime, limestone and It is preferable to use one or more selected from the group consisting of cement.

On the other hand, the organic and inorganic waste resources reprocessed by the method of the present invention can be effectively used in various fields such as landfill material, compost for landfill according to the type and purpose of the organic and inorganic waste resources introduced.

Specifically, Figure 1 is a photograph showing a process of treating sewage sludge in the organic and inorganic waste resources according to the present invention. More specifically, FIG. 1A is a sewage sludge having one kind of organic / inorganic waste resources, and an appropriate ratio of ferrous sulfate and calcium oxide is simultaneously added to the sewage sludge in FIG. 1B. Figure 1c is a photograph showing the exothermic reaction by reacting the injected material and sewage sludge, Figure 1d is a photograph showing that the exothermic reaction is maintained even after one day.

2 is a photograph showing a process of treating purified sludge in organic / inorganic waste resources according to the present invention. More specifically, FIG. 2A shows purified sludge having one kind of organic / inorganic waste resources. In FIG. 2B, ferrous sulfate and calcium oxide in an appropriate ratio are simultaneously added to the purified sludge. Figure 2c is a photograph showing the exothermic reaction by reacting the injected material and sewage sludge, Figure 2d is a photograph showing that the exothermic reaction is maintained even after one day.

3 is a photograph showing that the present invention can be applied to food waste among organic and inorganic waste resources, FIG. 3A is a photograph of food waste, which is a kind of organic and inorganic waste resources, and FIG. 3B is the food waste. It is a photograph which shows that ferrous sulfate and calcium oxide of an appropriate ratio are simultaneously added to the film.

Hereinafter, the present invention will be described in detail by way of examples. The following examples are merely illustrative of the present invention, but the scope of the present invention is not limited to the following examples.

<Example 1>

At room temperature, 35 parts by weight of ferrous sulfate (purchased from Cosmo Chemical) and 20 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of sewage sludge, followed by stirring to prepare a cover material for landfill.

<Example 2>

A cover material for landfill was prepared in the same manner as in Example 1 except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of sewage sludge.

<Example 3>

A cover material for landfill was prepared in the same manner as in Example 1, except that 20 parts by weight of ferrous sulfate and 10 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of sewage sludge.

Comparative Example 1

A cover material for landfill was prepared in the same manner as in Example 1 except that ferrous sulfate and calcium oxide were not added.

Comparative Example 2

A cover material for landfill was prepared in the same manner as in Example 1 except that 10 parts by weight of ferrous sulfate and 5 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of sewage sludge.

Comparative Example 3

A cover material for landfill was prepared in the same manner as in Example 1, except that 40 parts by weight of ferrous sulfate and 30 parts by weight of calcium oxide were added simultaneously with respect to 100 parts by weight of sewage sludge.

<Example 4>

A cover material for landfill was prepared in the same manner as in Example 1, except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of purified sludge.

Example 5

A landfill material for reclamation was prepared in the same manner as in Example 1, except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of the pulverized powder (wall thickener).

<Example 6>

A landfill material for landfill was prepared in the same manner as in Example 1 except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of food waste.

<Example 7>

A cover material for landfill was prepared in the same manner as in Example 1, except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of the steel sludge.

<Example 8>

A cover material for landfill was prepared in the same manner as in Example 1 except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were added simultaneously with 100 parts by weight of waste gypsum.

Example 9

A cover material for landfill was prepared in the same manner as in Example 1, except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were added simultaneously with 100 parts by weight of waste lime.

<Example 10>

A covering material for landfill was prepared in the same manner as in Example 1, except that 27.5 parts by weight of ferrous sulfate and 12.5 parts by weight of calcium oxide were simultaneously added to 100 parts by weight of dredged soil.

 Experimental Example

Examples 1 to 10 and Comparative Examples 1 to 3, the change in water content, pH and odor of the landfill covering material over time was measured and the results are shown in Table 1. The degree of odor was measured by sensory evaluation by giving a score of 1 to 5 after 5 people absorbed (1 means no odor, 5 means very bad odor) was expressed by the average value.

Before input 12h 24h 36h 48h pH stink Example 1 78.2 59.2 46.7 39.9 30.2 7.62 2.09 Example 2 78.4 59.2 48.5 43.2 34.5 7.33 2.12 Example 3 77.5 64.4 50.1 46.4 38.6 7.41 2.24 Comparative Example 1 77.4 72.8 68.0 63.7 59.2 8.72 4.32 Comparative Example 2 78.5 68.5 56.1 49.2 44.1 8.31 3.31 Comparative Example 3 79.1 56.5 43.2 37.3 27.5 9.45 4.32 Example 4 74.1 58.2 47.5 41.8 33.2 7.21 2.31 Example 5 58.2 51.7 46.2 39.0 30.1 7.24 2.34 Example 6 69.7 61.0 52.6 44.1 34.4 7.31 2.36 Example 7 56.5 46.9 40.0 35.5 27.4 7.27 1.89 Example 8 51.8 44.1 38.0 33.2 26.6 6.32 2.17 Example 9 49.7 43.9 38.1 33.0 27.1 7.93 1.98 Example 10 52.5 45.0 41.9 36.6 30.5 7.34 1.92

However, the pH was measured after 48 hours. The figure represents the moisture content (%)

Table 1 is a value obtained by measuring the change in moisture content after a certain period of time. As can be seen from the above results, the present invention minimizes odor while solidifying various organic and inorganic waste resources in a short time. On the other hand, in the case of Comparative Example 3, the reaction proceeded very quickly by adding an excess amount of ferrous sulfate and calcium oxide, but the reaction itself proceeded too fast, making it difficult to control the reaction, and very difficult to separate the silo and the cover material. Difficulties were observed. In addition, there was a limit to remove the odor because it is difficult to maintain the proper pH.

According to the method for reprocessing organic / inorganic waste resources according to the present invention, time and cost savings due to process shortening are achieved by directly reacting sulfate compounds and strong alkaline powders with organic / inorganic waste resources to be reprocessed without preparing a solidifying agent. In addition, it can be widely applied to various organic and inorganic waste resources such as sewage sludge, food waste, and livestock waste. In addition, since sulfate compounds and strong alkaline powders can use wastes, they are very effective for resource utilization, and if the pH is properly maintained, odors from organic and inorganic waste resources can be effectively removed. In addition, the organic and inorganic waste resources treated by the present invention can be widely used as landfill material, landfill and compost.

Although the present invention has been described in detail only with respect to the embodiments described, it will be apparent to those skilled in the art that various modifications and variations are possible within the technical spirit of the present invention, and such modifications and variations belong to the appended claims. .

Claims (8)

A method for reprocessing organic / inorganic waste resources, characterized by solidifying and deodorizing the organic and inorganic waste resources by simultaneously introducing sulfate compounds and strong alkaline powders into the organic and inorganic waste resources. The method of claim 1, The organic and inorganic waste resources are any one selected from the group consisting of sewage sludge, purified sludge, food waste, livestock waste, waste gypsum, waste lime and dredged soil. Way. The method of claim 1, 20 to 35 parts by weight of the sulfate compound and 10 to 15 parts by weight of a strong alkaline powder are added to 100 parts by weight of the organic / inorganic waste resources. The method of claim 3, The injected sulphate compound and the strong alkali-based powder is a weight ratio of 6: 4 to 7: 3 of the organic-inorganic waste resources reprocessing method. The method of claim 3, The reprocessing process is a reprocessing method of the organic and inorganic waste resources, characterized in that proceeding at pH 6 ~ 8. The method of claim 1, The sulfate compound is calcium sulfate (CaSO ₄ ), potassium sulfate (K ₂ SO ₄ ), sodium sulfate (Na ₂ SO ₄ ), ferrous sulfate (FeSO ₄ ), ferric sulfate (Fe ₂ (SO ₄ ) ₃ ) and its hydrates The organic and inorganic waste resources reprocessing method, characterized in that any one or more selected from the group consisting of. The method of claim 1, The strong alkali-based powder is any one or more selected from the group consisting of calcium oxide, magnesium oxide, quicklime, slaked lime, limestone and cement, the organic and inorganic waste resources reprocessing method. A reclaimed cover material comprising organic and inorganic waste resources reprocessed by the method of any one of claims 1 to 7.

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