KR100841335B1 - Development on the utilization and fuelization technologies of organic wastes such as piggery waste, food waste and swage sludge using cogeneration system including high pressure steam drying, gasification and power generation processes - Google Patents

Abstract

An apparatus and a method for treating swine waste having severe odor and a water content of at least 90% discharged from a pig farmhouse by using high pressure steam are provided, and a cogeneration system including high pressure steam drying, gasification and power generation by using the apparatus is provided to produce a compost and a solid fuel from swine waste treated using high pressure steam, and produce electric power by passing the solid fuel through gasification equipment. An apparatus for drying livestock waste or organic waste using high pressure steam comprises: an injection port(21) for supplying livestock waste including swine waste, or organic waste; a reactor(22) drying the livestock waste or organic waste with supplied high pressure steam while agitating the livestock waste including swine waste, or organic waste that has been supplied through the injection port by an agitator(221) axially connected to a rotary shaft(251); a double jacket(23) installed to cover an outer portion of the reactor so as to insulate thermally the reactor; a high pressure steam supply unit(24) that supplies high pressure steam for breaking cell walls of the livestock waste supplied into the reactor; a rotating unit(25) for rotating the agitator; a reactor rotating unit(26) for rotating the reactor; a discharge unit(27) penetratingly connected to a bottom part of the reactor through the double jacket to discharge treated livestock waste or organic waste; and a control box(28) for controlling the rotary speed and the steam supply amount of the reactor.

Description

Livestock manure or organic waste drying apparatus using medium pressure steam and method for drying livestock manure or organic waste using same and cogeneration apparatus including high efficiency drying / gasification of livestock manure or organic waste using such livestock manure or organic waste drying apparatus on the utilization and fuelization technologies of organic wastes such as piggery waste, food waste and swage sludge using cogeneration system including high pressure steam drying, gasification and power generation processes}

Figure 1a is a block diagram of the organic waste (livestock manure, sewage sludge and food waste) treatment and recycling process according to the present invention,

Figure 1b is a self-contained eco-friendly ecological system to be built through the present invention,

Figure 2 is a livestock manure or organic waste drying apparatus diagram using medium pressure steam according to the present invention,

3 is a schematic diagram of a reactor rotating apparatus for livestock waste or organic waste drying apparatus using medium pressure steam according to the present invention;

4 is a diagram illustrating a mechanism for improving drying performance of livestock waste or organic waste drying apparatus using medium pressure steam according to the present invention;

Figure 5a is an embodiment showing the weight change before and after livestock manure drying treatment using livestock manure or organic waste drying apparatus according to the present invention,

Figure 5b is an embodiment showing the odor change according to the livestock manure or organic waste drying treatment time using livestock manure or organic waste drying apparatus according to the present invention,

FIG. 6 is a process diagram of a gasifier for producing electric power by molding the solid product after the livestock manure or organic waste drying treatment using livestock manure or organic waste according to the present invention.

<Description of the symbols for the main parts of the drawings>

(1): solid-liquid separator
(2) livestock manure or organic waste drying equipment

(3) Solid fuel manufacturing equipment (4) Gasifier

(5): power production equipment (6): steam production equipment

(7): Boiler (8): Reformer

(9) High temperature air production part (10) Syngas purification part

(11): gasifier high temperature air supply (21): inlet

(22): reactor 23: double jacket

(24): medium pressure steam supply means (25): rotation means

(26): reactor rotation means (27): discharge means

(28): control box (91): heat exchanger

(92): blower (93): combustor

101: filter 102: cleaner

(111): heat exchanger (112): blower

(221): stirring device (231): medium pressure steam supply port

241: main supply line 242: decompression line

(243): double jacket insulation supply line (251): rotating shaft

252: Bearing 253: Pulley

(254): motor pulley (255): motor

(261): reactor axis of rotation (262): sprocket

(264): Worm Gear (265): Lever

2511: nozzle

The present invention provides a livestock manure or organic waste drying apparatus using medium pressure steam and a method for drying livestock manure or organic waste using the same and cogeneration including high efficiency drying / gasification of livestock manure or organic waste using such livestock manure or organic waste drying apparatus. Relates to a device.

Increasing national income has led to diversification, quality and mass production and consumption of social members, especially meat consumption through changes in dietary culture. Accordingly, the livestock industry, including pigs, chickens, and cattle, has grown in size with increasing number of heads to meet the demand.

However, such economic development seriously raises the problem of pollution of living environment, which must be overcome in order to realize pleasant and prosperous human life.

With the recent development of intensive livestock farming, the annual discharge of domestic livestock manure is about 45 million tons, serving as an enormous fertilizer resource, and on the other hand, also recognized as a pollution source of the surrounding environment. Due to concerns about the cause of soil and water pollution, odors and pests caused by pissing, demands and interests on livestock manure treatment and environmental problems are increasing in the surrounding area and society.

As of 2005, the number of pigs raised as a substitute for beef and chicken has reached 8,830,000 heads due to mad cow disease and highly pathogenic avian influenza.

However, the number of breeding heads began to decrease after peaking in September 2003, despite the fact that the price of pig farms was high. It is evaluated.

In addition, the dumping of organic wastes is scheduled to be banned after 2010 under the Marine Pollution Prevention Act, and the difficulties of livestock farms are expected to increase even further. This was also reflected in the 2003 Management Survey conducted by the Swine Association. The survey found that the biggest difficulties of the swine workers were in the order of manure treatment, difficulty financing, poor balance of payment, and protection. The priority of the project was investigated in order of resource manure recycling, odor prevention measures and disease prevention.

Half of domestic hog farms maintain 1,000 to 1,200 heads and produce 10 to 15 tons / day of manure. Treatment of the discharged manure is carried out by marine discharge, treatment using public facilities, or fermentation treatment using a moisture control material which is inexpensive and expensive.

Livestock manure has been managed in the framework of the Law on Sewage and Livestock Wastes, focusing on water quality management, including purification, and recycling in individual farming units, and composting solid components, purifying liquid components and surroundings. Efforts are being made to develop a variety of eco-friendly technologies to resolve complaints caused by odor problems.

In Korea, the treatment of livestock manure from cattle barns is usually done by marine discharge, treatment using public facilities, and composting with moisture control materials such as sawdust and rice husk, but there are still many difficulties. .

In other words, livestock manure can contribute to environment-friendly agriculture such as soil improvement (physical, chemical and biological) in addition to pure fertilizer function, but it is unfavorable in the competition with chemical fertilizer due to the imbalance of fertilizer components and high cost and labor when spraying. It is difficult to resource fertilizer.

In addition, livestock manure is a high concentration of organic substances, and in the process of processing and bad odor generated in the process of neighboring residents complaints, and some unsanitary house management may increase the environmental pollution.

Farms that have difficulty in recycling livestock manure have installed purification treatment facilities, but they are often higher in concentrations than general sewage or factory wastewater, causing technical and economic difficulties, and increasing cases of improper treatment or unauthorized discharge due to neglect of farm management. to be.

In addition, in the case of public facilities, the throughput is less than the capacity ('03, operation rate 64.5%), and the treatment efficiency is lowered due to the inflow of high concentration of mixed manure and aging due to premature corrosion of the facility. The system is inadequate.

Moreover, the installation of public treatment facilities is also perceived as hateful facilities, and there are cases where delays are caused due to opposition of residents and passive promotion of local governments when selecting locations.

In addition, the operational aspects of livestock manure treatment facilities include the rise in price and difficulty in supply and demand for moisture control materials (sawdust, etc.), premature aging of facilities and equipment, and the ability to self-treat more than breeding heads. ㆍ Activation of natural circulation system through livestock farming is not working well.

In addition, even in farms that depended on the discharge of manure for various reasons, such as disposal costs or the hassle of effort, the government is considering a policy to reduce waste discharge by the government according to the international agreement on waste discharge. If so, it is essential to develop economical and environmentally friendly technologies for the treatment of livestock manure from livestock houses.

As part of measures to solve this problem, the government has expanded the method of treating organic wastes such as incineration, composting, solidification or solidification, carbonization, and cement kiln, establishing new resource processing facilities (liquid and compost production), and establishing integrated regional management centers. However, despite these measures, frequent complaints due to bad smells have made it difficult to expand livestock farms or processing facilities.

In addition, most of the organic waste treatment is made by anaerobic digestion process, the development of electric power production technology using methane gas by domestic and foreign fermentation of organic waste.

However, in the case of the development of the resourceization technology by anaerobic digestion process, 30-40 days are required for gas generation, and it is difficult to secure enough space for treatment and stable gas generation as well as still have a complaint of odor. I'm holding it. In addition, residual sludge after treatment of organic waste using the existing anaerobic digestion process has been dumped at sea until now, but since 2010, the secondary treatment using the drying / gasification / power generation system related to the present invention is carried out as a total prohibition of ocean dumping. It is essential.

An object of the present invention for solving the above problems is to use pig steam manure which is the main culprit of continuous complaints and water pollution due to the moisture content and severe odors of more than 90% discharged from livestock farms, especially pig farms To provide an apparatus and method for processing.

In addition, another object of the present invention is a cogeneration device including a medium-pressure steam drying / gasification / power generation to produce electric power through the fertilizer and shaping the treated pig manure using medium pressure steam, the solid fuel is again a gasifier To provide.

In addition, another object of the present invention is an apparatus and method for treating organic waste (food waste, sewage sludge) as well as livestock manure including pig manure using medium pressure steam and solid fuel, and the solid fuel is again through a gasifier The present invention provides a cogeneration device using medium pressure steam to generate electric power.

The present invention to achieve the object as described above and to solve the conventional drawbacks is to feed livestock manure or organic waste into a reactor of a constant size to supply a medium pressure steam to increase the temperature and pressure in the reactor 180 ~ 200 By maintaining the temperature of 17 ~ 20 atm, by treating the internal water contained in the cell wall of the solid waste, the water content can be reduced to about 30%, as well as to remove most of the odor component. As such, after treating pig manure or organic waste using heavy steam, the solid and liquid waste may be used as a good compost. In addition, the excess solid waste after treatment is about 4,000 kcal / kg calorific value can be produced by combustion or gasification power. Therefore, through the present invention, it is possible to secure the competitiveness of domestic pig farms, preserve the water environment, and create an eco-friendly self-developed pig farm.

Hereinafter, the configuration and the operation of the embodiments of the present invention will be described in detail with reference to the accompanying drawings.

Figure 1a is a schematic diagram of the livestock waste treatment and recycling process according to the present invention, Figure 1b is a self-contained eco-friendly ecological system to be constructed through the present invention, as shown the device configuration and process of the present invention is a high function As a constitution for reducing water, removing odors, and recycling resources using low energy such as livestock manure, the cogeneration device of livestock waste can use biomass or organic waste as well as livestock manure including pig manure as raw materials. That is, single or mixed use is possible.

Specifically, the cogeneration apparatus of the present invention comprises: a solid-liquid separator 1 which receives at least one of livestock manure, biomass, and organic waste; Livestock manure that receives any one or more of livestock manure, biomass, and organic waste from the solid-liquid separator, destroys any cell membrane among livestock manure, biomass, and organic waste supplied by drying and treating Organic waste drying apparatus (2); Solid fuel manufacturing apparatus for solidifying a portion of any one or more of livestock manure, biomass, and organic waste dried in the livestock manure or organic waste drying apparatus (2) and fertilizing a portion not used as fertilizer (3) Wow; A gasifier 4 for gasifying the solid fuel produced through the solid fuel manufacturing apparatus; A power production device 5 for producing electric power using the syngas supplied through the gasifier and a steam production device 6 for producing steam; It comprises a boiler (7) for supplying steam to the livestock waste or organic waste drying apparatus (2).

In addition, the steam production device 6 supplies steam so that the steam generated during incineration with the low calorific gas boiler is connected to any one point of a line for supplying steam to the livestock manure or the organic waste drying apparatus 2. The line was constructed. The gas generated in the gasifier is syngas (CO + H ₂ ) having a calorific value of about 1,300 kcal / Nm ³ .

The method for drying livestock manure or organic waste including pig manure using the above-described device configuration is provided with livestock manure or organic waste drying apparatus, and then supplying medium pressure steam into the reactor to control the internal conditions of the reactor at 180 to 200 ° C, It destroys the cell membranes of livestock manure or organic waste containing pig manure maintained at 17 to 20 atm and dries it to the internal water of the cells, thereby drastically lowering the water content to 30%, and then preparing a synthesis gas using a fixed bed gasifier. It is possible to manufacture electric and heating steam for self-generation, and the dried solid and liquid products can be used as high-quality organic fertilizer with odors removed. Therefore, it is easy to build eco-friendly ecological system through drying and gasification using livestock manure. It becomes possible.
In the above method of maintaining the internal conditions of the reactor at 180 to 200 ° C. and 17 to 20 atm, using a thermometer and a pressure gauge commonly used in a reactor using pressurized steam, a medium pressure supplying medium pressure steam to the inside of the reactor is performed. The temperature and pressure in the reactor may be adjusted through the main supply line 241 of the steam supply means 24 and the decompression line 242 for discharging the medium pressure steam. That is, by controlling the main supply line 241 and the decompression line 242 of the medium-pressure steam supply means 24 according to the target temperature and pressure, if the temperature and pressure is low, additional supply through the main supply line 241 and If the temperature and pressure are high, the pressure may be reduced by using the decompression line 242. The thermometer for measuring the internal temperature and the pressure gauge for measuring pressure, which are commonly used in a device such as a reactor, may be constructed in various ways, and thus detailed descriptions thereof will be omitted.

2 is a diagram of a livestock manure drying system using medium pressure steam according to the present invention, Figure 3 is a schematic diagram of a reactor rotating device of a livestock manure or organic waste drying apparatus using a medium pressure steam according to the present invention, as shown, Livestock manure sludge with a water content of 80 to 90% separated through a liquid separator is dried and treated in a livestock manure or organic waste drying apparatus. In the present invention, the livestock manure drying or organic waste drying apparatus of FIG. 2 is introduced to improve the efficiency of the existing medium-pressure steam drying system and to reduce drying performance and energy cost. In general, the medium pressure steam drying system rotates the rotor blade inside the reactor for mixing the livestock manure and steam supplied into the reactor, whereas in the present invention livestock manure or organic waste drying apparatus to increase the mixing efficiency of the drying system of FIG. As can be seen from the side view, a gear system for rotation was installed outside the reactor, and the reactor itself was designed to rotate.

As shown in the configuration of the present invention, in the livestock manure or organic waste (food waste, sewage sludge) drying device containing pig manure,

An inlet port 21 for supplying livestock manure or organic waste including pig manure; A reactor (22) for drying livestock manure or organic waste including pig manure supplied to the inlet (21) with a medium pressure steam supplied while stirring with a stirring device (221) condensed to the rotary shaft (251); A double jacket (23) installed to surround the outside of the reactor for insulation; Medium pressure steam supply means (24) for supplying medium pressure steam for destroying the cell walls of livestock manure supplied into the reactor; Rotating means (25) for rotating the stirring device; Reactor rotating means (26) for rotating the reactor; A discharge means (27) passing through the double jacket (23) and connected to a lower portion of the reactor (22) to discharge dried livestock manure or organic waste; It comprises a control box 28 for controlling the rotational speed of the reactor, the amount of steam supply.

The double jacket 23 includes a medium pressure steam supply port 231 penetrating the double jacket so that the medium pressure steam is supplied to the space between the double jacket and the reactor for the insulation of the reactor.

The inside of the reactor is configured to be maintained at 180 to 200 ℃, 17 to 20 atm by the supply of medium pressure steam. When the temperature and pressure inside the reactor are outside the range of 180 to 200 ° C. and 17 to 20 atm, the reactivity is very low, so that it is difficult to effectively control the moisture content and odor, and when maintained above the temperature and pressure, there is no significant change in the moisture content and odor control. In addition, the operation cost of the livestock should increase according to the type of livestock manure or organic waste to be introduced.

Rotating means 25 for rotating the stirring device is a rotating shaft which is equipped with a stirrer around the penetrating through the reactor and configured to eject into the reactor through a nozzle 2511 formed on the surface of the medium pressure steam ( 251); Bearings 252 for supporting both sides of the rotation shaft; A pulley 253 coupled to a rotating shaft 251 penetrating one of the bearings; A motor pulley 254 for transmitting power to the pulley 253; It consists of a motor 255 for transmitting power to the motor pulley.

Reactor rotation means for rotating the reactor 26 is formed on both sides of the double jacket coupled to the reactor and interlocked on both sides, the reactor rotating shaft (261) is a shaft coupled to the hollow shaft formed therein; A sprocket 262 formed at one end of the reactor rotating shaft; A worm gear 264 gear engaged with the sprocket; It consists of a lever 265 for rotating the worm gear.

The medium-pressure steam supply means 24 includes a main supply line 241 configured to connect steam supplied from the boiler 7 and the low calorific gas boiler 6 to one axis of the reactor rotating shaft 261; A decompression line 242 which is branched at one side of the main supply line and connected to the upper part of the reactor so as to decompress it; Branched from one side of the main supply line is composed of a double jacket insulation supply line (243) for supplying medium pressure steam into the double jacket.

As described above, the present invention improves the drying treatment performance while increasing mixing by rotating the reactor itself as well as mixing using the rotary blades inside the reactor.

In addition, the outside of the reactor is composed of a double jacket to supply steam at the processing temperature during the treatment into the double jacket to increase the thermal insulation effect. This can reduce the operating cost by reducing the amount of steam condensed in the supplied steam.

By applying livestock manure or organic waste drying device using medium pressure steam, it is possible to obtain a solid product of stable quality using minimum water vapor. Up to 30% of this solid product can be made. In particular, it is possible to reduce sulfur compounds (hydrogen sulfide, methyl mercaptan, methyl sulfide, methyl disulfide, etc.), which are major odor components of livestock manure, which are the biggest cause of complaints, to 1/10 to 1/100. The reduction of sulfur compounds, which are a major malodorous component of livestock manure, is thought to be due to the Mailride reaction that proceeds above 130 ° C.

The livestock manure or organic waste containing pig manure is charged to the reactor of the livestock manure or organic waste drying apparatus at a filling rate of 50%, preheated using the supplied saturated steam for 30 to 60 minutes, and then stirred when the reactor reaches a predetermined temperature. The apparatus is stirred for 30 minutes, after which the gas generated from the inside of the reactor is released for 10 minutes, and the released gas is cooled and condensed in the condenser and then supplied to the purification system.

Each of the numerical values was determined through experiments, and the most preferable result was obtained in the numerical interval. The condensation purification system is omitted in the drawing.

On the other hand, the treated solid waste in the reactor is recovered from the outside after opening the discharge means of the reactor.

The dried and treated livestock manure using the medium pressure steam has a characteristic of water content of about 30%, calorific value 4,000kcal / kg through natural drying, and pelletized using a molded fuel manufacturing apparatus.

Figure 4 is a mechanism of improving the drying performance of livestock waste manure or organic waste drying apparatus using medium pressure steam according to the present invention, Figure 5a is a weight change after the drying treatment using a livestock manure or organic waste drying apparatus using a medium pressure steam according to the present invention 5B shows an exemplary view showing a change in odor according to drying treatment time using livestock waste manure or organic waste drying apparatus according to the present invention, as shown in the livestock manure Alternatively, when using the organic waste drying apparatus, the crushing effect of the medium pressure steam of 180-200 ° C. and 17-20 atm is generated, and thus the surface area for water evaporation can be increased compared to the conventional drying method including hot air or natural drying. In addition, the destruction of cell walls leads to the drying of internal water that cannot be discharged in nature. Can.

The heavy vapor steam drying treatment example of the present invention is as shown in Figures 5a, 5b.

First, as shown in FIG. 5A, it can be seen that the weight change after the drying and treatment using the medium pressure steam was greatly reduced after about 30 hours. Therefore, it is possible to confirm the change of the water content according to the cell disruption effect by the drying method using the heavy steam of the present invention.

In addition, as shown in FIG. 5B, the change in odor caused by sensory odor measurement is significantly reduced after diluting fold after treatment for about 30 minutes.

As a result, dried and treated livestock manure using medium pressure steam has a characteristic of about 30% moisture content and calorific value of 4,000kcal / kg through natural drying without supplying additional heat source.

6 is a process diagram of the gasification of the solid product after the livestock waste drying treatment using medium pressure steam according to the present invention, Figure 1b is an embodiment of a fixed bed gasifier according to the present invention, Figure 8 is a self-contained eco-friendly to be built through the present invention 6 shows an ecological system diagram, which is pelletized using a livestock manure or a new waste molded fuel manufacturing apparatus dried by the livestock manure or organic waste drying apparatus of the present invention as shown in FIG. 6. The gasification system shown produces syngas (CO + H ₂ ) having a calorific value of 1,300 kcal / Nm ³ .

Specifically, the gasifier 4 according to FIG. 6 includes a reformer 8 connected to the gasifier to reform gas quality; It heat-exchanges with the heat exchanger 91 which supplies the high temperature air to the reformer 8, and burns some gas which passed through the scrubber while being heat-exchanged with the blower 92 and the heat exchanger 91 connected by the connection pipe to generate high-temperature air. A high temperature air production unit (9) consisting of a combustor (93); Synthesis gas purification unit 10 consisting of a filter 101 for filtering the hot gas supplied from the reformer 8 and a scrubber 102 for cleaning the gas passing through the filter and supplying the gas to the power production apparatus 5. )Wow; Gasifier high temperature air supply unit 11 is composed of a blower 112 for heat exchange with the heat exchanger 111 formed in the connection pipe between the filter and the scrubber of the syngas purification unit 10 to supply the hot air to the lower portion of the gasifier. It is configured to include.

Synthetic gas (CO + H ₂ ) having a calorific value of about 1,300 kcal / Nm ³ generated through the gasifier of FIG. 6 is used to produce steam and electricity by using an incinerator or an engine (Duel fueled engine, stirling engine or diesel engine). do.

The electricity and steam produced in this way can be used for self-generation and heating, and some of the steam can be used as steam to be re-supplied to livestock manure or organic waste drying equipment so that no additional steam supply is required. can do.

In addition, the treatment of livestock manure with liquid fertilization is to spread the liquid manure to farmland. The maturation process can be divided into the anaerobic method of completely anaerobic fermentation to produce methane and the aerobic method of decomposing organic matter by continuously supplying air. Odor problems due to liquid liquefaction occurs a lot when spraying, if you are a mature liquid fertilizer problem is not serious, but if the unspoiled manure is sprayed because the bad smell is very severe must be sprayed fermented liquid fertilizer.

In the case of wastewater treated with livestock manure or organic waste drying apparatus using medium pressure steam, the odor is already removed, which can greatly improve the odor during the housing process and spraying, and block the possibility of parasite contamination when feeding and using livestock manure. Dies when heated for more than 1 minute at 65 ℃ or higher), so it can be used as liquid solution directly. In other words, considering that the circumferential farming preferences for livestock farmers are increasing because natural circulation farming methods using livestock manure are continuously expanding and disseminating, it would be possible to smoothly manure livestock manure in connection with nearby farming farmers. do.

The present invention is not limited to the above-described specific preferred embodiments, and various modifications can be made by any person having ordinary skill in the art without departing from the gist of the present invention claimed in the claims. Of course, such changes will fall within the scope of the claims.

The present invention as described above has the advantage of high efficiency, low-cost livestock manure treatment, and converts the livestock manure of high function (more than 90 wt.%) Into a solid product of low water content (30 wt.%) In a short time to compost The advantage of increased usability, the high possibility of liquefaction of odor-free liquid wastes, the possibility of blocking the possibility of parasite contamination through livestock manure treatment at high temperature, and livestock manure by linkage with breeders It is possible to visualize the spread of environment-friendly farming and increase farm productivity through recycling, reduce the livestock manure cost, and secure domestic competitiveness of domestic livestock farmers, and suggest alternatives to marine discharge restriction of livestock manure. It is expected to reduce burden on livestock farmers and revitalize livestock industry by resolving complaints caused by odors. The advantage of the smooth and efficient use of livestock houses through the simplified process, the reduction of livestock waste treatment costs, the prevention of diseases through the improvement of livestock livestock environment, and the seasonal heat and electricity through combustion and gasification using solid waste. It is a useful invention with the advantage that it is possible to supply environmentally friendly ecological farms because it is possible to supply loads.

Claims (12)

In the drying device of livestock manure or organic waste containing pig manure, An inlet port 21 for supplying livestock manure or organic waste including pig manure; A reactor (22) for drying livestock manure or organic waste including pig manure supplied to the inlet (21) with a medium pressure steam supplied while stirring with a stirring device (221) condensed to the rotary shaft (251); A double jacket (23) installed to surround the outside of the reactor for insulation; Medium pressure steam supply means (24) for supplying medium pressure steam for destroying the cell walls of livestock manure supplied into the reactor; Rotating means (25) for rotating the stirring device; Reactor rotating means (26) for rotating the reactor; A discharge means 27 penetrating through the double jacket 23 and connected to a lower portion of the reactor 22 to discharge treated livestock manure or organic waste; Livestock manure or organic waste drying apparatus using medium pressure steam, characterized in that it comprises a control box 28 for controlling the rotational speed of the reactor, the amount of steam supply. The method of claim 1, The double jacket 23 is a livestock using a medium pressure steam, characterized in that it comprises a medium pressure steam supply port 231 through the double jacket so that the medium pressure steam is supplied to the space between the double jacket and the reactor for the insulation of the reactor Manure or organic waste drying apparatus. The method of claim 1, Inside the reactor, the temperature and pressure in the reactor are 180 to 200 ° C. and 17 to 20 atm through the main supply line 241 of the medium pressure steam supply means 24 for supplying the medium pressure steam and the decompression line 242 for discharging the medium pressure steam. Livestock manure or organic waste drying apparatus using medium pressure steam, characterized in that configured to be maintained as. The method of claim 1, Rotating means 25 for rotating the stirring device is A rotating shaft 251 equipped with a stirring device around the reactor and configured to blow into the reactor through a nozzle 2511 formed on a surface of the medium pressure steam supplied through an inner hollow portion; Bearings 252 for supporting both sides of the rotation shaft; A pulley 253 coupled to a rotating shaft 251 penetrating one of the bearings; A motor pulley 254 for transmitting power to the pulley 253; Livestock manure or organic waste drying apparatus using medium pressure steam, characterized in that consisting of a motor 255 for transmitting power to the motor pulley. The method of claim 1, Reactor rotation means for rotating the reactor 26 A reactor rotation shaft 261 formed on both sides of the double jacket coupled to and interlocked at both sides of the reactor, and the rotation shaft being axially coupled to a hollow formed therein; A sprocket 262 formed at one end of the reactor rotating shaft; A worm gear 264 gear engaged with the sprocket; Livestock manure or organic waste drying apparatus using medium pressure steam, characterized in that consisting of a lever 265 for rotating the worm gear. The method of claim 1, The medium pressure steam supply means 24 is A main supply line 241 configured to connect steam supplied from the boiler and the incinerator to one shaft of the reactor rotating shaft 261; A decompression line 242 which is branched at one side of the main supply line and connected to the upper part of the reactor so as to decompress it; Livestock manure or organic waste drying apparatus using a medium pressure steam, characterized in that consisting of a double jacket heat insulation supply line (243) branched from one side of the main supply line to supply the medium pressure steam into the double jacket. In the method of drying livestock manure or organic waste containing pig manure, After the livestock manure or organic waste drying apparatus according to any one of claims 1 to 6, including the pig manure supplied by supplying a medium-pressure steam of 180 ~ 200 ℃, 17-20 atm supplied from the boiler inside the reactor A method of drying livestock manure or organic waste using livestock manure or organic waste drying apparatus, characterized by breaking the cell membrane of livestock manure or organic waste to dry up to the internal water of the cells. The method of claim 7, wherein The livestock manure or organic waste containing pig manure is charged to the reactor of the livestock manure or organic waste drying apparatus at a filling rate of 50%, preheated using the supplied saturated steam for 30 to 60 minutes, and then stirred when the reactor reaches a predetermined temperature. Agitate for 30 minutes with the apparatus, and then discharge the gas generated from the inside of the reactor for 10 minutes, the released gas is cooled and condensed in the condenser and supplied to the purification system, livestock manure or organic waste Method of drying livestock manure or organic waste using a drying device. In the cogeneration device of livestock manure or organic waste using any one or more of livestock manure, biomass, organic waste containing pig manure, Receives any one or more of livestock manure, biomass, and organic waste from the solid-liquid separator (1) is configured to destroy any cell membrane of livestock manure, biomass, organic waste supplied by heavy-pressure steam treatment to dry to internal water Livestock manure or organic waste drying apparatus (2) according to any one of claims 1 to 6; Any one of livestock manure, biomass and organic waste dried in the livestock manure or organic waste drying apparatus (2) is used as a fertilizer and solid fuel manufacturing apparatus (3) for solidifying a portion not used as a fertilizer; ; A gasifier 4 for gasifying the solid fuel produced through the solid fuel manufacturing apparatus; A power production device 5 for producing electric power using the syngas supplied through the gasifier and a steam production device 6 for producing steam; It includes a high efficiency drying / gasification of livestock manure or organic waste using a livestock manure or organic waste drying apparatus, characterized in that it comprises a boiler (7) for supplying steam to the livestock manure or organic waste drying apparatus (2) Cogeneration device. The method of claim 9, The steam producing device 6 is a low calorific gas boiler and any one of the lines for supplying steam generated by the combustion of syngas, which is low calorific gas, to the livestock manure or the organic waste drying apparatus 2; A cogeneration device comprising high efficiency drying / gasification of livestock manure or organic waste using livestock manure or organic waste drying apparatus, characterized in that the steam supply line is configured to connect. The method of claim 9, The gas generated in the gasifier is a combined gas comprising a high efficiency drying / gasification of livestock manure or organic waste using livestock manure or organic waste drying apparatus, characterized in that the synthesis gas. The method of claim 9, The gasifier 4 is A reformer 8 connected to the gasifier to reform gas quality; It heat-exchanges with the heat exchanger 91 which supplies the high temperature air to the reformer 8, and burns some gas which passed through the scrubber while being heat-exchanged with the blower 92 and the heat exchanger 91 connected by the connection pipe to generate high-temperature air. A high temperature air production unit (9) consisting of a combustor (93); Synthesis gas purification unit 10 consisting of a filter 101 for filtering the hot gas supplied from the reformer 8 and a scrubber 102 for cleaning the gas passing through the filter and supplying the gas to the power production apparatus 5. )Wow; Gasifier high temperature air supply unit 11 is composed of a blower 112 for heat exchange with the heat exchanger 111 formed in the connection pipe between the filter and the scrubber of the syngas purification unit 10 to supply the hot air to the lower portion of the gasifier. A cogeneration device comprising high efficiency drying / gasification of livestock manure or organic waste using livestock manure or organic waste drying apparatus comprising a.

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