KR20130125953A - Food waste to produce a de-icing salt device and method for it's - Google Patents

Abstract

The present invention relates to an apparatus and a method for producing a deicing agent using food waste which uses high temperature gas generated from carbonizing solid parts of the food waste for drying leachate of the food waste, and salt generated from a drying process as the deicing agent for roads. The apparatus for producing the deicing agent using the food waste comprises the following: a crushing device crushing the food waste; a solid-liquid separation device washing the solid parts of the food waste containing high contents of salt with low salinity washing water and clear water, and separating the result into solid and liquid; a food waste leachate preprocessing apparatus inserting a coagulating agent for removing organic matter and solid particles from food waste leachate separated from the solid-liquid separation device; a gas collection device having condensation heat for evaporating moisture and concentrating salt which dissolved in the food waste leachate; a deicing agent generation device adding chemicals to the concentrated salt to obtain the deicing agent; a drying furnace for drying the deicing agent; and a packaging facility.

Description

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for producing a snow remover with food waste,

In the process of coalification of solid matter in food waste, the waste heat of the generated hot gas is used as a source of external heat energy necessary for salt concentration process of food waste leachate (hereinafter referred to as "negative waste water & The organic and fine particles contained in the waste wastewater are separated by flotation using a flocculant in the pretreatment process of the water treatment process, and are recycled as renewable ecological coal through the coalification process, The salinity remained in the treatment process relates to an apparatus and a method for producing a snow remover using food waste for use as a de-icing salt for thawing roads freezing in the winter season.

Although the waste water generated during the pretreatment process for recycling food waste contains a large amount of organic matter, fine particles and salinity, it is not technically easy to properly treat the waste water and recycle it. In addition, due to the high cost of disposal, it has been used in the deep sea for economic reasons. However, in accordance with the London Convention, which is effective from 2013, each country has to change the existing marine dumping method to land treatment have.

In addition, the majority of conventional food waste disposal companies are small and medium-sized enterprises, and the accumulation of the processing technology is low, and since there is not enough capital to invest, the above-mentioned waste water is more economically and cheaply used It is necessary to have a technology capable of processing such information.

Prior art to reduce the volume of food waste by using microorganisms is the influence of salt concentration on food waste disposal by Park Seungjo and others.

In the above prior art, the food waste generally contains about 3% of the salt content (compared with the dried material), and the experiment using the salt resistant Bacillus strain shows that the microbial activity is significantly lowered at 12.5% .

Therefore, when extracting and concentrating salinity (at least 3% ~ maximum 15%) from food wastes by biological treatment process, it has big problems in process.

Particularly, since the methanogenic microorganisms are more sensitive to the salt concentration in the fermentation process, the biogas recycling of the wastewater is not efficient and the problem of treating the residual wastewater after the biogas production may occur at the same time. In the recycling process, non-biological, physical and chemical methods should be applied.

However, if the organic matter and salt contained in the waste water are not completely removed, the environment can be deteriorated, and a method of reducing the environmental pollution along with an active recycling plan should be sought.

In the present invention, in order to remove organic matter and solid particulate matter from the wastewater in the present invention, the organic wastewater contained in the wastewater is separated and floated by flocculation or flocculation, and the residue is finally filtered and purified do.

However, in case of water treatment by sedimentation, a settling tank should be installed, and a process of separating and removing moisture from the precipitated sediment is further needed.

On the other hand, in order to precipitate the fine particles and the organic matter, it is possible to use a metal-based coagulant having a high specific gravity such as an iron salt or an aluminum, and further use sand, clay or the like to accelerate the precipitation.

However, the use of the organic coagulant-containing organic material as a raw material for the coalification process may cause controversy regarding the heavy metal content in the coalification recycle process, .

Therefore, in the present invention, a method of using a polymer flocculant as a raw material for a coalification process together with concentrated organic and fine particles is applied.

A final filtration water purification method, a fiber filtration apparatus using a fiber (fiber or fiber) material as a filter medium, a filtration apparatus using sand or anthracite as a filtration material, or a filtration carrier for other filters utilizing coal or a porous inorganic medium The filter can be applied according to the characteristics of the medium to be filtered.

However, in the case of a filtration apparatus using a filter medium having a cavity, it is necessary to provide a backwashing apparatus for backwashing due to the occlusion phenomenon caused by the filter cake layer deposited on the upper layer, It is disadvantageous to frequently change the filter medium because the filter medium of the filter cake layer which is not improved is to be removed.

As a technology that can treat a large amount of water in a short time, it can be treated by using a membrane. In this case, MF (Microfiltration) and UF (Ultrafiltration: ultrafiltration) There is a method of maximizing the efficiency, and a stepwise combination membrane processing method in which organic and solid particulates are separated from each other and RO (Reversed Osmosis) is combined to treat the remaining salt can be utilized as a method of combining MF and UF .

In addition to the advantages of obtaining high-quality filtered water through the separation membrane method as described above and having a high processing capacity compared to the scale of the apparatus, the maintenance cost is high due to the short life of the membrane and high unit cost, There is a disadvantage that the initial installation cost is high.

In addition, since a large amount of salt is still present in the filtered water (treated water) from which the organic matter and the solid particulate are removed through the pretreatment process for treating the wastewater, there is a technique for removing the dissolved salt remaining in the filtered water, Devices or ion exchange resins can be utilized.

In the case of the electrolytic apparatus, there is a disadvantage in that the efficiency of the used electric power is lowered due to the use of a rectifier for converting the AC power to DC, and the electrode plate used as the electrode is disassembled or destroyed and needs to be frequently replaced.

Further, in the case of using the electrolytic apparatus, since the efficiency of electrolysis can be reduced when the impurities remain, there is a restriction condition that a device having a high filtration efficiency is required at the front end.

In the case of ion exchange resins, the development of the exchange resins has progressed to some extent, but it has been possible to apply them even in the mixed state of foreign matters. However, if the exchange ability of the ion exchange resin deteriorates, If the frequency is increased frequently, the exchange ability is remarkably reduced and the ion exchange resin must be replaced.

In addition, there is a distillation method as a technique for completely extracting and separating the salt, and the distillation method has an advantage that it can be applied as a simple device, but it has a disadvantage that it consumes a large amount of energy.

However, in the present invention, energy consumption can be reduced by recycling the waste heat generated in the coalification process of food waste and distilling the salt of the waste water to concentrate the salt.

The organic and solid particulates removed by the above-mentioned conventional wastewater treatment method can be recycled in conjunction with each other. However, except for the distillation method in which extracted water is evaporated to extract only salinity, And follow-up measures are needed.

Among the prior arts disclosed in the patent documents, the 'facility for treating liquid waste of food waste wastewater' (Registered Patent No. 10-0918112) is a technology for liquefying the waste water, which uses multi-stage aeration equipment to remove waste water from aerobic fermentation But it does not use any chemical or coagulant. Therefore, it has the advantages of quality preservation effect and odor reduction, but there is no separate technology to remove salt from the final product, There is a problem that the salt concentration is increased.

In addition, 'a waste water treatment system in which a waste water treatment plant and a sewage treatment plant are connected' (Patent Application No. 10-2011-0006757) is a technology for catalytic oxidation treatment of waste water, And the biodegradable materials of the fat component contained therein are advantageously recycled as cleaning water for solid-liquid separator by water treatment using catalytic oxidation water. However, in order to lower the concentration of saline contained in the washing liquid, There is a disadvantage in that the demand for clear water required for salinity dilution is high and the diluted water still contains salt. Therefore, when used as recycling water for washing, there is a problem that equipment to be washed is corroded.

In addition, the above method has the possibility that the ecosystem is contaminated by salinity when it is released to rivers.

On the other hand, the technology disclosed in the 'Food Waste Treatment Apparatus' (Registered Patent No. 10-1039269) is a technique to dry the food waste by using a heating burner. The food waste is dried by utilizing a high temperature heating burner, It is advantageous that it can be quickly dried and recycled as a feed through recycling of steam heat generated during drying of waste and recycling of heat of communication of burner. However, the equipment structure for utilizing waste heat or latent heat is complicated and the waste water is utilized by burner communication heat In the case of evaporation, the inner wall of the heating part is clogged due to the organic matter and solids contained in the wastewater and the odor is generated, and it is impossible to recycle the organic matter and salt contained in the wastewater.

In order to process and recycle efficient waste water, it is necessary to pre-treat the organic matter and the fine particles contained in the waste water as a raw material for the recycling process technology to produce recycled coal.

This is to increase the production efficiency in the recycling process in which water is removed and concentrated in the dissolved salt still remaining in the pretreated waste wastewater as a snow remover, and as a treatment technique for this purpose, A combined technique of applying a purification treatment technique and combining a distillation method for concentrating the salt present in the negative wastewater in ionic form is applied.

Accordingly, it is an object of the present invention to provide a method for producing condensed heat of a high-temperature gas generated in a coalification process for food wastes as an external heat source necessary for concentrating the salt contained in the wastewater, And it is an object of the present invention to provide an apparatus and a method for recycling organic wastes generated by the pretreatment of waste wastewater as useful fuel (recycled coal) of energy resources together with solids of food wastes .

As a means for achieving the above object, the present invention provides an apparatus for producing negative wastewater from food wastes as a snow removing agent, comprising: a shredding device for supplying and disrupting food waste; A solid-liquid separator for separating a solid containing a high concentration of salt into a solid and a liquid after washing with a low concentration (saline) washing water and fresh water; A negative wastewater pretreatment device for injecting a coagulant to remove foreign matter such as organic matter, particulate solid matter and the like contained in the liquid material (wastewater) separated from the solid-liquid separation device; A gas collecting device for receiving a high-temperature and high-pressure gas containing condensation heat for evaporating and concentrating the moisture and salt dissolved in the negative wastewater from which foreign substances such as organic matter have been removed; A snow removers generating device for adding a chemical agent to concentrated saline by using the condensation heat to generate a snow remover; A drying furnace for drying the produced snow remover; And a packaging equipment for packaging the dried snow remover.

Here, the gas collecting apparatus is a system in which the condensation heat generated in the coalification process for producing recycled coal from organic matter and solid particulate matter removed from the waste water through the solid matter separated from the solid-liquid separator of the food waste and the waste water- And is a device for concentrating the salt contained in the pretreated waste wastewater and recycling it as an external heat source required to convert (produce) the concentrated salt into a snow remover.

The negative wastewater pretreatment apparatus for removing foreign matter includes a storage tank for storing waste water to be introduced into a foreign matter removing process such as organic material and fine particles mixed with a flocculant; A transfer control valve for controlling the operation of the water level control sensor and the flow meter to check the amount of waste water flowing from the storage tank and to adjust the quantity to be pretreated; A feed pump mounted on the storage tank for feeding the waste water from the storage tank to the waste water pretreatment process; A coagulant supply pump for supplying coagulant to the negative wastewater conveyed by the elevation transfer pump; A mixing device for mixing the supplied waste water and the flocculant; A reaction tank for coagulating and reacting the wastewater to which the coagulant is added to form an organic material in a floc form and supplying microbubbles to the microorganism; A scum storage tank for filtering and separating the scumped organic material lumps; And a filter for removing foreign substances which are not processed in the scum storage tank.

In addition, the construction of the reaction tank for treating the negative wastewater includes: a compressor for supplying high-pressure air into the device (reaction tank) for generating minute bubbles; A scum removing device mounted on the upper part of the apparatus and including a scum removing blade for collecting floating scum; A scum reservoir mounted on one side of the reaction tank for storing scum removed; And a micro bubble generator including a nozzle for generating micro bubbles using the high-pressure air supplied from the compressor.

Meanwhile, a method of producing a snow remover with food wastes includes a step (S 1) of feeding and crushing food wastes to be supplied and crushing the supplied food wastes; A wet cleaning step (S2) of wetly cleaning solid matter containing a high concentration of salt with wash water and fresh water of a low concentration (salt); A solid-liquid separation step (S3) of wet-washing and separating into liquid and solid; (S4) a negative wastewater pretreatment step (S4) for removing foreign substances such as organic substances contained in the negative wastewater by administering coagulant to the wastewater containing sodium chloride and sodium chloride, A step S5 of concentrating the water to evaporate water by heating the waste water to 100 DEG C or higher using the heat of condensation of the hot gas at 250 DEG C in the pre-treated liquid waste water; A chemical adding step (S6) of adding and mixing a chemical agent to the concentrated saline; (S7) of producing a liquid snow remover by stirring a mixture of concentrated saline and an added chemical agent while supplying condensation heat; A solid snow remover producing step (S8) of producing the resulting liquid removers through a drying process at about 200 DEG C and producing solid snow removers; And a packaging step S9 of packaging the finished snow remover.

The present invention has the effect of providing technical alternatives to establish the basis for the land treatment of food waste by developing production processing technology for coalification of food waste prohibited from the marine dumping in 2013, It has the advantage of eliminating the marine pollution factors such as marine pollution and the death of marine water resources.

In addition, by producing recycled coal that can be used as an energy fuel from organic waste, it is advantageous to acquire the energy source and at the same time, the recycled coal produced provides ease of maintenance such as storage and transportation, There is also the advantage that it is a wide-area energy source without.

The production of recycled coal from organic wastes is effective in treating organic wastes since the organic wastes are constantly generated in everyday life, and at the same time, the supply of raw materials is stably performed, so it is easy to secure coal resources as a solid type energy fuel At the same time.

The present invention provides a coalification production process capable of producing food waste from recycled coal in a short period of time, thereby preventing odor from being generated due to long-term accumulation of food waste and also helping to prevent the occurrence of waterborne communicable diseases.

In addition, the present invention improves the coalification production process to an intermittent continuous batch production process, thereby minimizing the size of the coalification production apparatus, and at the same time, improving the productivity of recycled coal.

In addition, the present invention has economical effect of recycling salt from wastewater as a snow remover, and it is possible to save a large amount of water by replacing the cooling water required for cooling the hot gas generated in the coalification production process with the wastewater.

In addition, since the water contained in the hot gas generated in the waste water cooling process becomes distilled water during the cooling process, a large amount of water can be saved through the use of the distilled water as washing water required in the production process, By recycling the waste heat generated in the coalification production process of external energy, the energy saving effect can also be expected.

Since the saline contained in the waste water used as the cooling water is recycled as the raw material for the snow remover, the water temperature of the salted water is increased by the condensation heat held by the hot gas during the cooling process and can be recycled as hot water.

Meanwhile, the present invention can be applied to food wastes which are operated in the existing food wastes disposal site, so that the solid waste can be coalized through the treatment of food wastes or the wastewater generated in saline washing can be produced as a snow removing agent Cost reduction is expected through utilization of the process installed in the existing treatment plant.

FIG. 1 is a schematic diagram of the entire treatment apparatus for the coalification process and the snow remover production process of the food waste according to the present invention,
FIG. 2 is a flowchart of a pretreatment process of the waste water of the present invention,
FIG. 3 is a process flow chart for producing the snow-removing agent by the coalification process and the negative wastewater of the present invention,
FIG. 4 is a process flow diagram for producing a snow remover with a negative wastewater according to the present invention.

Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. In describing the present invention, the same technical structures as those of the prior art will be given the same names as they are.

1 to 3, an apparatus for producing a snow remover with food waste according to the present invention comprises a shredding apparatus 10 for supplying and disrupting food waste; A solid-liquid separator (40) for separating a solid containing a high concentration of salt into a solid and a liquid by wet cleaning with low concentration (saline) washing water and fresh water using the principle of osmotic pressure; A negative wastewater pretreatment device 20 for injecting a coagulant to remove foreign substances such as organic matter and particulate solid matter contained in the liquid material (waste water) separated from the solid-liquid separation device; A gas collecting device (30) containing condensation heat for concentrating saline by evaporating water to concentrate the saline dissolved in the negative wastewater from which foreign substances such as organic matter have been removed; (60) for adding a chemical agent (6) to concentrated salt by using the condensation heat to produce a snow remover; A drying furnace (70) for drying the produced snow removers; And a packaging facility 80 for packaging the dried snow remover.

2, the negative wastewater pretreatment apparatus 20 includes a negative wastewater storage tank 21 for storing negative wastewater to be introduced into a foreign matter removing process such as organic material and fine particles mixed with a coagulant; A feed control valve 22 for controlling the operation of the water level control sensor and the flow meter to check the amount of waste water flowing from the waste water storage tank 21 and adjust the amount of waste water to be pretreated; A feed conveyance pump 23 mounted on the waste water storage tank 21 to feed the waste water supplied through the feed control valve 22 from the waste water storage tank 21 to the waste water pretreatment process; A flocculant supply pump (24) for supplying flocculant to the negative wastewater conveyed by the elevation transfer pump (23); A mixing device (25) for mixing the supplied waste water and the flocculant; A water treatment tank 26 in which a compressor 261 for supplying fine bubbles and a scum removing device 262 for removing scum are installed to coagulate the negative wastewater to which the coagulant has been added to make the organic matter floc; A scum storage tank (263) for filtering and separating the scumped organic material mass; And a filter group 28 for removing foreign matter not processed in the scum storage tank 263.

Here, the filter group 28 for removing foreign matters remaining in the purified wastewater through the coagulation treatment process is a filter combination composed of a final filtration filter 281 and a cleaning filter 282, The filter 282 is suitable for the pretreatment of the final filtration filter 281. The final filtration filter 281 is suitable for a metal strainer having excellent corrosion resistance and capable of determining whether to install the filter according to the concentration of the residual foreign matter after the water treatment. It is preferable to have a back-washing function as a filter made of a fiber material.

The water treatment tank 26 for removing scum from the processed wastewater is provided with a compressor 261 for supplying high-pressure air to the inside of the apparatus (reaction tank) for generating minute bubbles; A scum removing device (262) mounted on the upper part of the apparatus and including a scum removing blade for collecting floating scum; A scum storage tank (263) mounted on one side of the water treatment tank (26) for storing scum removed; And a micro-bubble generator 264 including a nozzle for generating micro-bubbles using the high-pressure air supplied from the compressor 261.

At this time, a backwashing water automatic control valve 1 "R is placed between the final filtration filter 281 and the cleaning filter 282, and a pre- (1 ").

As shown in FIG. 1, the gas collecting device 30 can operate the coalification production process in an intermittent continuous production mode by linking with the coalification reaction tank 50, and a specific structure thereof is a cylindrical structure An inner tube (31); And an outer cylinder 32 for circulating cooling water to the outside of the inner cylinder 31 so as to cool the high temperature and high pressure gas is provided in the inner cylinder 31. The high temperature gas generated in the coalification and aging step is fed to the inner cylinder 31, A gas feed pipe 33 for feeding the gas; A gas discharge pipe 34 for discharging the cooled gas; A thermometer (T) and a pressure gauge (P) for measuring temperature and pressure; A gas control valve 4 is installed at the inlet side of the gas transfer pipe 33 and the discharge pipe 34 and a condensate control valve 4 is provided at the lower end of the device. 2) is mounted.

As shown in FIG. 3, the method of producing the snow remover with the food wastes includes a step (S 1) of injecting and crushing the garbage to be supplied and crushing the supplied food wastes; (S2) a wet cleaning step of wet-cleaning solid matter containing a high concentration of salt with low-concentration (saline) washing water and fresh water; A solid-liquid separation step (S3) of wet-washing and separating into liquid and solid; (S4) a negative wastewater pretreatment step (S4) for removing foreign substances such as organic substances contained in the negative wastewater by administering coagulant to the wastewater containing sodium chloride and sodium chloride, A step S5 of concentrating the water to evaporate water by heating the waste water to 100 DEG C or higher using the heat of condensation of the hot gas at 250 DEG C in the pre-treated liquid waste water; A chemical adding step (S6) of adding and mixing a chemical agent to the concentrated saline; (S7) of producing a liquid snow remover by stirring a mixture of concentrated saline and an added chemical agent while supplying condensation heat; A solid snow remover producing step (S8) of producing the resulting liquid removers through a drying process at about 200 DEG C and producing solid snow removers; And a packaging step S9 of packaging the finished snow remover.

The chemicals used in the production of the snow remover include calcium carbonate (CaCO ₃ ), calcium sulfate (CaSO ₄ ) and clay as main components, and magnesium sulfate (MgSO ₄ ), calcium chloride (CaCl ₂ ) It is preferable to add magnesium chloride (MgCl ₂ ) and Kainite.

Hereinafter, the detailed description of the technology for recycling food waste as recycled coal fuel (prior art application No. 10-2011-0147046, 10-2011-0076797) will be omitted, but a coalification aging process (coalification reaction tank) A method and apparatus for producing negative wastewater as a snow removing agent by utilizing the heat of condensation generated in the wastewater treatment plant will be described in detail.

In order to recycle food waste into recycled coal, the process of selectively removing foreign substances such as metal, wood, vinyl, glass, ceramics, plastic, fiber, etc. contained in food waste should be preceded.

This applies not only to coal recycling equipment with large processing capacity, but also to unit sites or private residential areas with low processing capacity.

In the absence of contaminants, it can interfere with the process of recycling coal ash, especially in the coalification aging process, which produces food waste as recycled coal.

In addition, if a hard material such as a crusher, a screw-type wet cleaning device, or a screw-type transfer device is stuck to a normal operation of the rotating body associated with each process, There is a high possibility of damage in the early stage.

In order to remove foreign matter, there is a method of removing iron-based metals using a magnet, a method of removing a nonferrous metal using a sensor, a solid solid removal method such as wood and plastic using a buoyancy, a specific gravity (wind sorter) or a sieve, Vinyl and fiber removal methods using hook hand are applied.

There is a method of removing foreign matter by complementing a device and a person by a method of extracting using a work force by a method other than the above.

In the present invention, as described above, it is assumed that the foreign substance contained in the food waste to be introduced is removed.

As shown in FIG. 1, the apparatus for feeding and crushing food waste into which the present invention is applied has a structure in which the apparatus is naturally dropped by gravity from the upper part to the lower part. A disk-shaped scalpel is a structure in which one or more sheets are fixed at regular intervals. The disk has protruding portions or holes, so that the food waste is crushed by the collision or broken by the blade formed in the perforated portion And a grinding machine 11 is mounted on the grinding wheel 11. The basic principle is to apply the conventional grinding method.

More precisely, the process is started by pushing it into the injection device by using a tool such as a pinching device or a spatula, and additional water is added when necessary.

At this time, the installation position or direction of the inlet is determined in consideration of the convenience of the operator in the coal-fired recycling apparatus to be produced so that the operator's copper line can be shortened and at the same time, .

In addition, food wastes are viscous and watery in their characteristics, and organic matter is easily decomposed by microorganisms, which can cause acidic corrosion.

Therefore, the structure of the inlet of the injection and crushing apparatus 10 is formed into a hopper shape having a gentle curved inclination. The material is made of PP, PE, PVC, etc., which are excellent in corrosion resistance, Plastics, or nonferrous metals such as stainless steel, copper, and aluminum.

The introduced food waste is pulverized to a predetermined particle size by the pulverizer 11 installed at the bottom of the pulverizer 10 to increase the efficiency of the wet cleaning process.

The pulverizer 11 to be applied here is not particularly specified in the present invention because it can be applied to any form such as a doubled screw manufactured on the market or a disc type applying the above-described millstone method.

The shredded food waste is subjected to a washing process for the purpose of removing the salt.

The washing process according to the present invention is for extracting salinity from recycled coal, which is the final product of solid food garbage, and it is believed that the salinity contained in the oxidation process containing salinity causes secondary environmental pollution caused by dioxin .

Accordingly, in order to sufficiently remove the salt contained in the solid matter of the food waste, it is possible to perform a wet cleaning process of a single stroke or a wet cleaning of a plurality of strokes of a two-stage three-stage.

In addition, fresh water is introduced from the outside for the wet cleaning process, and the shredded food waste is transported.

For this purpose, a feeding screw device can be introduced. A nozzle device is installed at the upper end of the screw conveying device to allow fresh water to flow, and a filtration body It is desirable to have a sieve.

The wet wastewater generated in this process may also contain solid particles from the organic and crushing process, including the salt extracted from the solid matter, and the wet washing process of the present invention may be performed by a single-stroke or two- Characterized by a process system for performing a plurality of strokes.

The saline-free solids from the wash step in the wash step have a high moisture content due to the moisture added to the food waste initially and the additional water for cleaning the wet scrubbing process.

Therefore, the solid-liquid separation step carried out after the washing step is introduced to remove the contained water because the energy consumption for recycling the highly water-soluble solid material as recycled coal fuel is high, which is not economical.

In addition, in order to perform smooth solid-liquid separation, the filter drawing net 41 surrounds the screw 42 provided at the center, and in order to separate solid-liquid separation, a scheme in which the interval of the pitch gradually decreases Or by adopting a double screw which operates with two screws meshing with each other, so that efficient dewatering can be performed in the progress process.

The solid-liquid separating step introduced here can be used as a separate independent stroke or as a conveying screw device introduced into the solid-substance conveying in the wet process.

A pretreatment apparatus for a foreign matter of solid matter is a device for introducing a catalyst, which is an essential element required in a coalification process, which is introduced for recycling food waste into recycled coal, and is introduced using a separate mix device (not shown) The solids mixed with solid-liquid separated solids or solid-liquid separated solids can be fed at a constant rate in accordance with the feed rate using a quantitative screw during the transfer to the coalization reactor for the coalification process.

Here, the pretreatment of the solid material means a process of removing foreign substances such as organic substances present in the liquid waste water from the solid-liquid separation, and the coalification reaction tank 50 is a process in which the separated solid material is aged It is a device to heat the solids by injecting energy from the outside and aging at high temperature and high pressure for a certain period of time to produce recycled coal.

By homogenizing the temperature of the sample using a screw type mixer provided with a stirring screw 51 rotating by a geared motor for stirring 52 for mixing the sample put into the coalification reactor 50, So that the recycled coal produced after aging is easily discharged to the outside of the coalification reaction tank 50.

In this case, semi-sequential production can be adopted. However, due to the high-temperature gas generated in the coalification reaction tank 50 during the coalification aging process, the inside of the coalification reaction tank 50 is in a state of high temperature and high pressure do.

At this time, an input control valve 3 for controlling the inflow amount is provided between the solid-liquid separator 40 and the coalification reaction tank 50.

Before the discharge of the recycled coal having undergone the coalification aging process, a coal gasifier 50 capable of receiving a high-temperature gas is used to secure a state of a pressure inside the coalification reactor 50, They shall be installed so that they are open to each other.

At this time, a safety valve 5, a thermometer T and a pressure gauge P are mounted for safe operation of the gas collecting device 30, and a cooling operation is performed to convert the high temperature gas into a pneumatic pressure.

The coalification reaction tank 50 and the gas collection device 30 are connected to each other so that the coalification production process can be operated in an intermittent continuous production mode.

The coalification reaction tank 50 of the present invention includes a screw type mixer, a safety valve, a thermometer T and a pressure gauge P, which are connected to the gas collecting device 30 and are equipped with a stirring screw and a driving motor, And the process is automatically controlled by the pressure and the temperature of the coalification reaction tank 50.

Here, a mechanical or electronic pressure gauge (P) and a thermometer (T) for controlling the process are attached to the coalization reaction tank 50 to block the energy injected from the outside at a given temperature and pressure, When the temperature and the pressure fall within a certain range of deviation, the external energy is injected again.

The gas collecting device 30 is a device for constructing the coalification production process into a continuous production process by receiving high-temperature high-pressure gas and steam generated in the process of aging the pretreated solid in the coalification reaction tank 50 with recycled coal .

The gas collecting device 30 is capable of cooling high-temperature and high-pressure gas and water vapor flowing through the dual structure to collect gas and water vapor at high temperature and high pressure in a container having a constant volume, It is possible to accommodate the expanded gas and the high-temperature gas containing water vapor in a container of a certain volume.

Therefore, the volume of the gas collecting device 30 is expanded to 1.2 to 6.0 times the net volume of the coalizing reaction tank 50 to reduce the instantaneous pressure applied to the gas collecting device 30, It is preferable to use a cooling device used for lowering the high pressure applied to the device 30, and to use the wastewater that has undergone the pretreatment process as cooling water in view of economy and environment.

In order to utilize the negative wastewater as the cooling water, the organic matter and the fine particles contained in the negative wastewater are removed before being introduced into the cooling water, so that the organic matter and the fine particles contained in the cooling water during the cooling process of the gas collecting device 30, And is adhered to the outer wall of the gas collecting device to lower the cooling efficiency and prevent odor from being generated.

Such impurities block the cooling water transfer pipe and cause a phenomenon that the cooling function is paralyzed. Therefore, the impurities such as organic matter are removed before they are introduced into the cooling water.

In order to remove organic and solid particulates from the waste water, a waste water pretreatment device is installed. In the waste water pretreatment device, salt dissolved in the ion state is not removed, so a separate process is required to remove the salt.

In the present invention, not only the saline is extracted and removed from the waste water, but is removed as a snow removing agent by injecting urea technology into the extracted salt.

Accordingly, the water is removed from the wastewater through the cooling and heat exchange process in which the temperature of the wastewater is increased to about 60 to 100 ° C or more through the heat exchange between the hot gas and the wastewater in the gas collecting device 30, Is performed.

The negative wastewater pretreatment device 20 removes organic matter and fine particles contained in the wastewater, more specifically, removes organic matter and fine particles from the wastewater, and cools the wastewater containing the residual salt in the ionic state And is used as cooling water for cooling the high-temperature high-pressure gas discharged from the aging step.

The principle of pretreatment of negative wastewater is a method of removing both fine particles and organic matter. It is a method of mixing fine wastewater with a coagulant and then mixing the wastewater. And remove it.

The scum removed wastewater is re-filtered to completely remove residual organic matter and fine particles, so that only the salt dissolved in the ionic wastewater remains in the wastewater.

The waste water pre-treatment apparatus 20 of the present invention includes a transfer control valve 1 for opening and closing the transfer amount of the waste water to automatically control the pretreatment process, a pretreatment control valve 1 "for controlling the transfer amount after the waste water pretreatment, , A backwash automatic control valve 1 '' R, and the like.

Here, the mass transfer of the waste water pre-treatment process proceeds from the negative wastewater transfer automatic control valve 1 to the automatic wastewater pretreatment automatic control valve 1 ".

On the other hand, the shape of the feed pump 23 for discharging the negative wastewater can be selected from a variety of products sold on the market.

The flocculant supply pump 24 is for introducing the flocculant. Since the flocculant is a liquid type, a tube pump, a tubing pump, a peristaltic pump, a metering pump, etc., which are commercially available, are used.

In this case, it is preferable that a predetermined amount is injected depending on the flow rate or flow rate of the incoming negative wastewater, and a digital type or an analog type and remote adjustment are possible, and the installation is preferably installed on the upper side of the channel to which the wastewater is transferred.

The negative wastewater and the coagulant mixer 25 are for mixing the negative wastewater to be conveyed and the coagulant introduced by the coagulant feed pump 24.

The mixing device 25 conventionally uses a stirring device that uses a power motor, but requires extra equipment and installation space as well as excessive power. Recently, the mixing device 25 is shown in FIG. 2 As described above, a partition wall 251 for obstructing the flow of the fluid is installed in the pipeline.

At this time, it is preferable to utilize a channel-type mixing apparatus that is easy to purchase in the market in consideration of economical efficiency as a simple method of forming a vortex by instantaneous expansion by increasing the diameter of the pipe.

The principle of generating and removing organic and solid particulate materials used in the waste water pretreatment process is as follows: floc is formed using a flocculant, microbubbles are injected thereinto, scrubbed and floated, and removed using a scum removing device Examples of the inorganic coagulant include aluminum sulfate (alumina sulfate), aluminum polychloride (PAC), aluminum polysulfate, ferric sulfate, ferric chloride, and organic coagulants. The coagulant can be classified into an inorganic coagulant and an organic coagulant. Polyamines, polyacrylamides, and the like.

Since these coagulants generally react sensitively to the pH (pH), considering that they are generally weakly acidic in the quality of the wastewater, aluminum sulfate is added to form a light floc, followed by flocculation by microbubbles or the like Here, sodium alginate, sodium silicate and the like may be used as coagulation assistants in order to promote the formation of flocs.

The micro-bubble generator 264 for injecting micro-bubbles into the formed flocs and scooping the micro-bubbles is installed at a lower end of one side of the water treatment tank 26. The micro-bubble generator 264 is connected to a commercially available compressor 261 The scum floated is collected in the scum storage tank 263 through the scum removing device 262 installed on the upper part of the water treatment tank 26, Is sent to the coalification reactor (50) for recycling as a raw material for the coalification process, resulting in recycled coal.

The water treatment tank 26 is a device for reacting negative coagulant with negative wastewater to form flocs and scooping the flocs using fine bubbles. The water treatment wastewater is disposed at one side of the lower end, A tubular mixing device 25, a micro-bubble generator 264 positioned at one side of the lower end or the middle part for pretreatment of the waste wastewater for flotation and separation; And a scum removing device 262 which is located at the upper end and is equipped with a blade for collecting generated scum on one side.

The waste water treatment tank 26 is provided with a float type scramper using power, a pipe type scum removing device for guiding the scum by cutting the pipe in half so that the scum generated by installing it on the upper end of the reaction tank can be introduced, A rotating type scum blade can be used as an auxiliary device for guiding the floated scum in one direction.

Here, the scum floated and separated are collected in the scum storage tank 263, and the removed scum contains an organic component. Therefore, the scum is fed into the coalification process of the solid food waste, And the waste generated in the waste water treatment process is coalized and recycled as energy.

The fine particles of the treated water treated in the water treatment tank 26 are removed by the coagulant and the fine bubbles, and the organic matter is also adsorbed on the coagulant and the fine particles, and the salt dissolved in the negative wastewater remains in the ionic form. A treatment process is required.

In this process, the dissolved salt is processed by the filtration equipment for the pre-treatment of the wastewater to be connected with the treatment process for the production of the snow remover, and then the high-temperature and high-pressure gas generated in the coalification reaction tank is captured by the connection process, The water contained in the gas collecting device is evaporated and concentrated.

At this time, utilizing the condensation heat generated from the gas collecting device, it is used as a raw material for producing the salt remaining after the pretreatment of the waste water.

The negative wastewater filter group 28 is composed of a final filtration filter 281 and a cleaning filter 282 for removing trace amounts of fine particles and organic matter remaining in the scum-removed wastewater treatment water.

For example, the final filtration filter 281 can reduce the load on the filter by using a filtration apparatus using a fiber as a filter medium, and construct a backwash system to enable backwashing if necessary.

The purpose of removing fine particles from the waste water pretreatment apparatus is to remove the soluble organic substances by using the property that the dissolved organic components are easily adsorbed to the particulate matter rather than the turbidity due to the particulates.

Therefore, in this principle, removal of fine particles from the wastewater to be maximally treated can remove not only turbidity but also soluble organic matter.

The strainer can be introduced into the filter for the cleaning filter 282. The filter can be introduced into the filter 282. The strainer can be introduced into the strainer according to the particle size of the fine particles remaining after the water treatment or the turbidity after the water treatment. It is preferable that the final filtration filter 281 is provided at the front end of the cleaning filter 282 for pretreatment.

The filters 281 and 282 are selected to be provided with a backwashing device so that they can be cleaned by fresh water because the air holes are blocked after a certain use time and the filtration function can not be performed.

At this time, the final filtration filter 281 and the cleaning filter 282 are operated such that the process water generated during the backwashing is fed back to the initial negative wastewater treatment process or put into the coalification recycling production process So that high-concentration concentrates can be recycled.

The treated water obtained in the negative wastewater pretreatment process is a state in which the organic matter and solids contained in the negative wastewater are removed and only the salt is contained and the residual water after the negative wastewater pretreatment After the salt is concentrated, it is used as a raw material for producing as a snow removing agent.

The process of producing pre-treated wastewater from wastewater as a snow remover is to add the necessary chemicals to the residual salt after the pretreatment process to make the wastewater as a snow remover and process it into a desired form to produce as a product.

The method of producing pre-treated wastewater as a snow removing agent is a method in which organic wastewater is dissolved in organic and solid particulate and ionic form and contains salt, so that organic wastewater and pre-treatment wastewater are removed, A pretreatment step (001) of a negative wastewater to obtain a negative wastewater containing; The pre-treated wastewater is introduced into the gas collecting device 30 which collects the hot gas at a temperature of 250 ° C or more as cooling water so that the collected hot gas is cooled and the negative wastewater supplied for cooling is introduced into the cooling water 002); After the temperature of the cooling water (negative wastewater) is raised up to 100 ° C or more to evaporate the moisture contained therein, the concentrated wastewater is concentrated and the wastewater that has been introduced into the cooling water is discharged to cool the wastewater Step (003); A chemical injection step (004) for injecting the chemicals necessary for the snow remover; (005) for producing a liquid snow remover by heating and stirring a mixture of concentrated saline and a chemical agent, and a step of producing the liquid removers by drying at a temperature of about 200 캜 and producing them as a solid phase type snow remover A solid phase snow remover production step (005), and a packaging step (005) in which the produced snow remover is wrapped and commercialized.

According to 'Green Product Information', a product production regulation for domestic eco-friendly commodity, there is a regulation that liquid heavy snow remover does not contain heavy metals and ethylene glycol.

In addition, the above guidelines should not exceed 20 weight (% by weight) and total amount of environmentally hazardous substance should not exceed 0.2 weight (% by weight) The quality of the product is certified by stipulating the solidification phase and the liquid phase respectively.

In the case of Europe, in Germany, the use of snowmelt or minerals as a guide for the production of traditional snowmobiles in the Winter Dienstleitfaden (Wege zur Feinstaubreduktion bei der Strassenstreuung) CaCl ₂ is added for the production of eco-friendly snow removers in consideration of the influence of ecosystem of sodium (Na). In order to maintain good contact with the road surface, snow removers are sprayed in liquid form do.

The present invention refers to the production instructions of these products in reference to the development of the process and apparatus technology for producing snow removers (NaCl) contained in the wastewater, and in particular, in the raw material making process of the waste water, It is possible to increase the content of salt by evaporating moisture in the process of using the pretreated wastewater as the cooling water of the gas collecting device 30 and add calcium (Ca) thereto to introduce a separate drying process if necessary .

The principle of producing the pretreated wastewater as a snow removing agent is to concentrate the salt (NaCl) of the pretreated wastewater containing a large amount of water in accordance with the production regulations and quality certification regulations of the domestic and foreign snowmelt products mentioned above, Is an environmentally friendly additive, calcium or calcium compound, to produce calcium chloride, which is then dried and produced.

The general main formula for producing snow removers is:

1) 2NH ₄ Cl + Ca (OH) ₂ ? CaCl ₂ + 2NH ₃ + 2H ₂ O

2) CaCO ₃ + 2HCl - > CaCl ₂ + CO ₂ + H ₂ O

3) CaCO ₃ + 2 NaCl → Na ₂ CO ₃ + CaCl ₂

Here, all three formulas (1), (2) and (3) can produce calcium chloride, and calcium chloride (calcium-based chemical) is added as a raw material to form calcium chloride.

The present invention produces calcium chloride, which is a snow remover, based on the above formula (3), separates sodium carbonate (Soda ash, Na ₂ CO ₃ ) and calcium chloride in a solution form, separates the condensation heat obtained in the gas collecting device (30) (Not shown), it is utilized as an external heat source required to produce a liquid snow removing agent by reacting with concentrated salt and added chemicals, and the produced liquid snow removing agent is introduced into a drying furnace (not shown) And the water is evaporated continuously to concentrate at a high concentration.

At this time, among the added salt, the remaining amount contributing to the production of the snow remover can be extracted in the form of salt, and the extracted salt is reused in the production process of the snow remover.

Through the production process of the snow remover, it is possible to produce about 40% of calcium chloride solution. The calcium chloride solution can be stabilized by controlling the acidity, and precipitates and impurities can be purified through the filtration process. In order to produce calcium chloride, 40% of the calcium chloride solution is dried in a drying furnace at a temperature of 200 ° C or higher.

In the method of producing the snow remover from the raw material of the pre-treated saline wastewater, the pre-treated wastewater is a state in which a large amount of moisture is contained when the snow remover is put into the raw material, and the concentration of the salt (NaCl) Is 1 to 35% or less, more accurately 3 to 12.5% or less). Therefore, by removing unnecessary moisture content from the raw material, the content of salt (NaCl) as a raw material of the snow remover can be concentrated to an appropriate concentration.

For this purpose, it is necessary to remove the water content from the pretreated waste wastewater containing the salt. For this purpose, the condensation heat is input from the gas collecting device to reduce the water content of the pretreated waste wastewater, Ca) chemical agent is added to the waste water to reduce the water content of the waste water by a calorific value (water is increased from room temperature to 60 ° C) generated when water and calcium (Ca) meet with each other, In the drying furnace where calcium chloride is produced and connected, it is dried at a temperature of about 200 ° C or higher to produce a snow removing agent.

CaCO ₃ , CaSO ₄ , clay, etc. are added as auxiliary chemicals, MgSO ₄ , CaCl ₂ , CaCO ₃ , Magnesium chloride (MgCl ₂ ), Kainite and the like are used.

An example of utilizing the pretreated waste water as the cooling water of the gas collecting device 30 is shown in FIG. 2 in which there is a gas collecting device 30 connected in the coalification reaction tank 50, and a waste water pre- And control valves 1, 1 "for pre-processing.

The purpose of installing the gas collecting device 30 here is to discharge the high-temperature and high-pressure gas generated during the coal aging process for producing recycled coal in the coalification reactor 50, This is to specify the improvement of productivity.

That is, when the coarse collecting device 30 is not installed, the production cycle of the coalification aging process is such that the raw material is charged and the coalification reaction tank is heated, and the coalification aging process proceeds under a certain condition for a certain period of time 10-2011-0076797). Through this, the coalification reactor saturated with the gas at high temperature and high pressure is gradually cooled, and the reactor is cooled And then discharging the recycled coal by opening and closing the coalification reactor. The estimated time will vary depending on the capacity of the reactor, but it takes about 8 ~ 24 hours. Therefore, when the gas collector is used, productivity is less than 3 hours It is significantly lower.

The purpose of cooling the gas collecting device 30 here is to accommodate a high-temperature and high-pressure gas having a volume expansion of 1260 times at a high temperature of 250 DEG C or more in a gas collecting device having a constant volume, The cooling principle is to use the pretreated wastewater at room temperature as cooling water to deprive the high-temperature high-pressure gas of the heat contained in the high-temperature gas through the amount of heating heat required to warm the cooling water to the vaporization point, The water vapor that is contained is condensed into water, and the high-temperature and high-pressure gas is decompressed (reduced in temperature) and discharged at a normal temperature and a normal pressure.

The total calorific value, which is the sum of the heating calorific value and the gasification calorific value applied to the cooling water, is the same as the amount of heat lost due to the conversion of the high-temperature high-pressure gas from the high-

The structure of the gas collecting device 30 for cooling the pretreated waste water is composed of an inner tube 31 of a cylindrical structure securing a space capable of diffusing to collect the hot gas and a cooling water circulating outside the inner tube 31 The gas collecting device 30 may be constructed in a single stage or in multiple stages. The gas collecting device 30 of the present invention may have a double structure, Structure.

The inner tube 31 is provided with a gas feed pipe 33 for feeding a high temperature and high pressure gas generated in the coalification tank 50, a discharge pipe 34 for discharging the cooled gas, a thermometer T and a pressure gauge P, And a safety valve (5) is mounted.

At this time, the gas transfer tube 33 of the inner tube 31 is inserted to the lower portion of the inner tube 31 to diffuse into the entire space of the inner tube 31.

However, due to the sudden cooling of the hot gas due to the condensate accumulated in the bottom of the inner cylinder (31), noise and vibration may occur, and cracks may be generated in the entire system connected with the vibration. Therefore, .

The method for cooling the pretreated waste wastewater in which the salt is dissolved in the ion trapping state in the gas collecting device 30 with the cooling water is a method in which the discharge pipe for the high temperature and high pressure gas generated in the coalification aging process is placed in the gas collecting device 30 at a condensate water level of 20 cm (Not shown) installed in the inner cylinder up to the lower end of the upper end of the condensed water to a height of about 10 cm in the condensed water level, Temperature and high-pressure gas is discharged to the gas discharge pipe provided at the upper end of the inner cylinder beyond the partition wall (not shown) to expand the space where the gas of high temperature and high pressure as possible stays in the inner cylinder of the gas collecting apparatus, , A pre-treated waste water pipe is connected to the lower end of the outer cylinder, which is the side where the discharge pipe of the high-temperature high-pressure gas of the gas collecting device 30 is inserted And the cooling water discharge pipe serves as a discharge pipe installed at the upper end of the outer pipe provided with the gas discharge pipe. The control of the cooling water volume controls the flow rate or the flow rate of the cooling water to the outlet temperature of the cooling water since the temperature of the introduced cooling water is increased through the cooling process.

The cooling process of the gas collecting apparatus 30 described above is performed by using the evaporation process using the heat of condensation of the gas collecting device 30 of the coalification process to recycle the pretreated waste water as a snow remover, By increasing the concentration, it is possible to reduce the energy required for the external heat source required in the evaporation drying process by recycling the condensation waste heat.

On the other hand, the composition of a malodor removal system (not shown) that can remove the malodors generated during the coalification process of the food waste and the production process of the snow remover of the negative wastewater is composed of a food waste disposal plant (coalification process and snow removal process) An air conditioning system for inhaling odor; A pretreatment filtration device for removing impurities contained in the condensed water while the high temperature and high pressure gas is cooled; An oxidizer generator such as an ozone generator for providing ozone with strong oxidizing power capable of decomposing the refractory material contained in the condensed water or a UV apparatus for irradiating UV rays; A biofilter filled with a microbial carrier to increase the density of the microbial population, the biofilter being operated by a biological process to remove residual odor components; A condensate pump for smooth transfer, and a gas pump or blower for transferring gas or odor components.

The function of the malodor removal system (not shown) is to remove the impurities contained in the high-temperature high-pressure gas through the pretreatment filtration device, remove the refractory substances contained in the condensed water from which the impurities have been removed by ozone or UV light, The condensate water is pumped from the top of the biofilter through a pump for pumping water and a feed pipe. The odor components flowing from the air conditioner in the work area of the coalification process of the coalification process and the coalification process of the food waste and the de- Through the biofilter and is processed by the biological treatment process and the washing process.

At this time, the condensed water that flows at the top of the biofilter acts as a moisture regulator of the washing process and the biofilter.

The amount of heat input to increase the salinity (NaCl) of the wastewater is about the utilization of the heat that the high-temperature and high-pressure gas discharged from the coal-aging process utilizes, that is, the heat of condensation, The energy efficiency of the total amount of energy input to the process is increased.

Here, the water vapor contained in the hot gas used to increase the concentration of saline in the wastewater is cooled and condensed and discharged, and the discharged condensate is treated through the biofilter and then used as washing water in the workplace, There is a saving effect.

The present invention relates to a recycling technology of raw waste water generated in the process of coalification treatment of food waste by the raw material of snow removers. The solid matter of the food waste and the fine particles and organic matter contained in the liquid material are recycled as recycled coal as the solid phase fuel, The amount of heat required to evaporate moisture to concentrate the saline contained in the liquid water (waste water) of the garbage is supplied to the gas collecting device The waste water contained in the high-temperature and high-pressure gas is recycled, the evaporated water is collected and recycled as the water in the workplace, and the moisture contained in the high-temperature and high-pressure gas is added to the odor remover (not shown) The entire process of the present invention can be constructed as a zero-discharge system.

The present invention as described above can be applied to the production of renewable energy recycling technology which produces solid and wastewater fine particles and organic matter of food waste that are prohibited from being dug out by 2013, By developing recycling technology, it is possible to provide an overall technical alternative to provide a basis for the treatment of food wastes on the ground, and to solve the problems of marine environment such as marine pollution caused by marine dumping of conventional food waste and the destruction of marine water resources. It has the environmental advantage of eliminating it.

In addition, by producing recycled coal, which is a solid fuel that is usable energy from food waste, there is a technical advantage that it is easy to maintain such as storage and transportation, and can acquire a wide-ranging energy source that is easy to use spatially and temporally.

Also, by supplying the recycled coal produced from the waste at a low cost through the present invention, the overall domestic energy cost is lowered, thereby enhancing the competitiveness of the product through the low production cost throughout the manufacturing industry.

The present invention is based on the development of a technology for pretreatment of waste wastewater containing a waste water treatment process and a technique for recycling saline contained in waste wastewater, , It is possible to eliminate the problem of odor due to long-term condensation of food wastes and to improve the water quality It also helps prevent the occurrence of infectious diseases.

In addition, through the combination of the system for linking the independent heating type coalification production system adopted by the present invention with the gas collecting apparatus, the coalification production process can improve productivity by constructing an intermittent automatic production system And the waste heat generated in the coalification process can be recycled.

In addition, when the gas collecting device having the cooling system is connected to the malodor removal system (not shown), the second environmental pollution caused by the exhaust gas generated in the coalification reaction tank can be prevented.

In addition, the present invention has an economical effect obtained by recycling salt from wastewater as a snow remover, as well as utilizing the wastewater as cooling water for high-temperature high-pressure gas generating negative wastewater, A large amount of water can be saved through recycling, and the energy saving effect by waste heat recycling can be expected in the production process of snow remover.

The present invention is also applicable to a food garbage disposal plant which is currently in operation, so that it is possible to save a budget by applying the system of the present invention to an existing apparatus constructed according to the present invention, And the effect of job creation for the production of the whole or partial apparatus for system management and system management.

The present invention relates to a method of recycling organic wastes generated from animal wastes including animal wastes, livestock manure containing a large amount of water, sewage sludge, food processing plant wastes, fermentation wastes, slaughterhouse wastes and leather processing plants to recycled coal as a solid fuel And can be utilized as a water treatment technology for proper treatment of waste water generated in the currently operated food waste disposal plant and further utilized as a recycling technology for the production of snow remover.

In addition, the present invention can be applied to industrial sites in which all industrial wastewater is generated, and it is possible to apply the technology used in the pretreatment process of the waste water to the wastewater of leather processing plants, It is possible to utilize it as a water treatment process in an industrial field where biological treatment can not be performed due to high content of organic matter and salt.

10: crushing device 20: waste water pretreatment device 21: waste water storage tank
25: mixing device 262: scum removing device 28: filter group
281: Final filtration filter 282: Cleaning filter
30: Gas collection device 40: Solid-liquid separation device 50: Coalification reaction tank
60: Snow remover generating device 70: Drying furnace 80: Packaging equipment

Claims (5)

A device for producing snow removers with food waste,
A crushing device (10) for supplying and disrupting food waste; A solid-liquid separator (40) for separating a solid containing a high concentration of salt into a solid and a liquid by wet cleaning with low concentration (saline) washing water and fresh water using the principle of osmotic pressure; A negative wastewater pretreatment device 20 for injecting a coagulant to remove foreign substances such as organic matter and particulate solid matter contained in the liquid material (waste water) separated from the solid-liquid separation device; A gas collecting device (30) containing condensation heat for concentrating saline by evaporating water to concentrate the saline dissolved in the negative wastewater from which foreign substances such as organic matter have been removed; (60) for adding a chemical agent (6) to concentrated salt by using the condensation heat to produce a snow remover; A drying furnace (70) for drying the produced snow removers; And a packing facility (80) for packing the dried snow remover. The device for producing snow remover with food wastes.
The method of claim 1,
The negative wastewater pretreatment device 20 includes a negative wastewater storage tank 21 for storing negative wastewater to be mixed with a coagulant to induce a foreign matter removal process such as organic matter and fine particles; A feed control valve 22 for controlling the operation of the water level control sensor and the flow meter to check the amount of waste water flowing from the waste water storage tank 21 and adjust the amount of waste water to be pretreated; A feed conveyance pump 23 mounted on the waste water storage tank 21 to feed the waste water supplied through the feed control valve 22 from the waste water storage tank 21 to the waste water pretreatment process; A flocculant supply pump (24) for supplying flocculant to the negative wastewater conveyed by the elevation transfer pump (23); A mixing device (25) for mixing the supplied waste water and the flocculant; A water treatment tank 26 in which a compressor 261 for supplying fine bubbles and a scum removing device 262 for removing scum are installed to coagulate the negative wastewater to which the coagulant has been added to make the organic matter floc; A scum storage tank (27) for filtering and separating the separated organic matter and solids; A final filtration filter 281 and a cleaning filter 282 constituting a filter group 28 for removing foreign matter remaining in the wastewater from which the coagulated organic matter and particulates are removed in the water treatment tank 26; In order to automatically control the waste water pre-treatment process, a transfer automatic control valve 1 for opening and closing the transfer amount of the negative wastewater, a control valve 1 "for controlling the transfer amount after the negative wastewater pretreatment, a backwash automatic control valve 1" And a device for producing a snow remover with food wastes.
The method of claim 1,
The gas collecting device 30 is operable to operate the coalification production process in an intermittent continuous production mode in cooperation with the coalification reaction tank 50. The gas collecting device 30 has a cylindrical inner pipe 31; And an outer cylinder 32 for circulating cooling water to the outside of the inner cylinder 31 to cool the high temperature and high pressure gas is provided in the inner cylinder 31 and a high temperature gas A gas feed pipe 33 for feeding the gas; A gas discharge pipe 34 for discharging the cooled gas; A thermometer (T) and a pressure gauge (P) for measuring temperature and pressure; And a safety valve (5) which is operated when a predetermined pressure is reached is mounted.
As a method of producing snow removers with food waste,
A step (S1) of feeding and crushing food waste to be supplied and crushing the charged food waste; A wet cleaning step (S2) of wetly cleaning solid matter containing a high concentration of salt with wash water and fresh water of a low concentration (salt); A solid-liquid separation step (S3) of wet-washing and separating into liquid and solid; (S4) a negative wastewater pretreatment step (S4) for removing foreign substances such as organic substances contained in the negative wastewater by administering coagulant to the wastewater containing sodium chloride and sodium chloride, A step S5 of concentrating the water to evaporate water by heating the waste water to 100 DEG C or higher using the heat of condensation of the hot gas at 250 DEG C in the pre-treated liquid waste water; (6) a chemical step (S6) of adding a chemical agent to the concentrated salt and mixing the chemical agent; (S7) of producing a liquid snow remover by stirring a mixture of concentrated saline and an added chemical agent while supplying condensation heat; A solid snow removing agent producing step (S8) of producing a liquid snow removing agent as a solid snow removing agent after drying at about 200 ° C .; And a packaging step (S9) for packaging the finished snow remover. The method for producing a snow remover with food wastes.
The method of claim 4.
The chemistry 6, calcium carbonate (CaCO _3), calcium sulfate (CaSO _4), clay, sulfate Marg when ium (MgSO _4), calcium chloride (CaCl _2), magnesium during ium (MgCl _2), Kainite chloride And a method of producing a snow remover using food waste.

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