A CARBONIZING TREATING APPARATUS FOR WASTE MATTER
FIELD OF THE INVENTION
The present invention relates to a carbonizing apparatus using far infrared rays; and more particularly, to a carbonizing apparatus using far infrared rays, which is capable of heightening a carbonizing efficiency through a direct heating system using a radiant heat of far infrared rays, shortening a working time through a speedy cooling process of carbonizing heat, and easily removing various kinds of noxious gas and bed smell etc. exhausted into the air.
DESCRIPTIONOFTHERELATEDART
In general, various kinds of wastes excepting of metal and wood etc., from home, a restaurant or an industrial field, and from a ship and hospital etc. is gathered by using a specific standardized bag for use in putting the wastes thereinto, etc., and is carried to a garbage fϊlled-up land etc., and then is processed by filling up it with the wastes. Such a general wastes process method pollutes soil and water, and furthermore requires a widespread reclamation land. Such a method is too limitary to process the wastes that is being gradually increased in a discharge quantity thereof, and causes a serious social problem. In recent, to solve such a conventional problem in a disposal of wastes, it is being widely used a carbonizing apparatus for heating and incinerating various kinds of wastes from a home, a restaurant and an industrial field etc. with heat of high temperature under a state of non-oxygen.
However, the conventional waste carbonizing apparatus being used
gradually widely utilizes an indirect heating method through a heater installed inside a carbonizing receptacle. Thus, such an apparatus has problems of unnecessarily, excessively, consuming power by much taking a temperature rise time to perform a carbonizing operation. Moreover, the conventional waste carbonizing apparatus has such a structural defect that carbonized matter should be discharged from the carbonizing receptacle after completing a carbonizing operation, thus a specific cooling device is not equipped therein. This requires a considerable working stand-by time till the carbonizing receptacle is naturally cooled and extremely drops an operation efficiency.
Furthermore, the conventional wastes carbonizing apparatus can't effectively remove various kinds of noxious gas and bad smell generated in the midst of carbonizing operation, which causes an atmospheric pollution and a difficulty in a widespread practical use.
SUMMARY OF THE INVENTION
Therefore, an object of the present invention is to provide a carbonizing apparatus using a far infrared rays heater, which is capable of extremely heightening an operation efficiency by shortening a temperature rise time necessary for a carbonizing operation through a direct heating method using a cartridge heater of far infrared rays, and thus preventing an unnecessary loss of power.
Another object of the present invention is to provide a carbonizing apparatus using a far infrared rays heater, which is capable of preventing a serious air pollution, by rapid cooling a carbonizing receptacle through a heat cooling
device so as to easily discharge carbonized matter, and simultaneously, by effectively removing various kinds of noxious gases and a bed smell generated in the midst of a carbonizing operation through a filtering unit having multi filtering steps. To achieve these objects, the carbonizing apparatus comprises a body case that has a door on one side face thereof, and has a far infrared rays heater and a carbonizing receptacle thereinside, the body case whose inner side wall faces are constructed of insulation bricks; a catalyst insulation of a tubular type, which has a dehumidifϊer, a catalyst heater, a catalyst alien-substance removal heater on an upper center portion of the body case, and which has a first catalyst, a second catalyst, a third catalyst, a fourth catalyst, a fifth catalyst, and a catalyst automatic temperature sensor in the inside thereof; an air tank of structure piped through the catalyst insulation, the air tank being constructed of a plurality of gas convection preventing plates; an auxiliary filtering device piped through the air tank, the auxiliary filtering device having a basic activated carbon, an acid activated carbon, and a neutral activated carbon in the inside thereof; a vacuum pump piped through the auxiliary filtering device, the vacuum pump being provided with an air generation pipe installed on one side thereof, and having an additional connection relation to an ozone generator as a separate construction; a water tank of structure into which the air generation pipe of the vacuum pump is inserted, the water tank being provided with a gas exhaust hole formed on an upper portion thereof; and an electron control panel device as a control unit, for controlling operations of a series of constructive parts.
BRIEF DESCRIPTION OF THE DRAWINGS
The above and other objects and features of the instant invention will become apparent from the following description of preferred embodiments taken in conjunction with the accompanying drawings, in which: FIG. 1 is a diagram showing a configuration of a carbonizing apparatus using a far infrared rays heater in accordance with the present invention;
FIG. 2 is a sectional view illustrating a main part of a body case in accordance with the present invention; and
FIG. 3 is a circuit diagram depicting an operation of a carbonizing apparatus using a far infrared rays heater in the present invention.
DETAILED DESCRIPTION OF THE EMBODIMENTS
Hereinafter, in accordance with preferred embodiments of the present invention, a carbonizing apparatus using a far infrared rays heater will be described in detail with reference to the accompanying drawings, as follows.
In accordance with the present invention, Fig. 1 shows a constructive diagram of a carbonizing apparatus using a far infrared rays heater, Fig. 2 shows a sectional view of a main part of a body case, and Fig. 3 shows an operating circuit diagram of the carbonizing apparatus using the far infrared rays heater. First describing an overall construction, a carbonizing apparatus includes a body case 1 having a far infrared rays heater 11 and a carbonizing receptacle 12 that are installed thereinside, a catalyst insulation 2, an air tank 3, an auxiliary filtering device 4, an ozone generator 5, a vacuum pump 6, and a water tank 7, and an electron control panel device 8 for operating and controlling these constructive
parts.
As shown in Fig. 1 or 2, the body case 1 has a door D of an open/close type like a refrigerator on one side face thereof. The body case 1 has an airtight structure of a rectangular shape having a constant internal space part. Its inner wall face is constructed of insulation bricks 13. Such an internal space is the structure connected to the body case 1. On one side upper part of the body case 1, a carbonizing temperature sensor (not shown in the drawings) and a cooling fan 14 operated by a driving motor M are formed, and on another side upper face symmetrical to the cooling fan 14, a blast suction opening 15 switched by a solenoid valve S is formed.
The far infrared rays heater 11 installed inside the body case 1 is made by filling up the inside of a stainless tube having a high durability with 100% ceramic alumina (AL203) having a high heat conduction, and then by inserting a heat line thereinto. Both ends of the heater 11 are connected to a power line, and are sealed up with a vacuum state. An outer view of such a constructed far infrared rays heater 11, namely, an outer face of the stainless tube is preferably coated with far infrared rays paints that is usable even at high temperature, e.g., 1200 degrees, so as to gain the far infrared rays ceramic cartridge heater.
The carbonizing receptacle 12 installed inside the body case 1 has structure that its upper part is opened as shown in Fig. 1. The carbonizing receptacle 12 is desirable to be constructed as a ceramic coating receptacle by coating the surface of the receptacle made of general Fe material with urethane of ceramic material.
Further, the catalyst insulation 2 is a filtering unit for primarily filtering various kinds of pollution gases, carbonated gas, generated in a carbonizing
operation. In the inside of such a catalyst insulation having a tubular type structure, it is formed a sequential accumulation structure of a dehumidifier 21, a catalyst heater 22, a first catalyst 23, a second catalyst 24, a third catalyst 25, a fourth catalyst 26, a fifth catalyst 27, and a catalyst automatic temperature sensor 28. A series of accumulated catalysts as the first through fifth catalysts are preferably provided with a catalyst alien-substance removal heater 29 that is installed on an outer side face thereof.
Herewith, the first catalyst 23 is the catalyst of an ammonia and amin group for use in removing a bed smell, and its chemical expression is as follows;
(#5 i- ) U&& 35CrcaH] (*l ) (IT)
(Ammonia) (Oxygen) 350°C catalyst (Nitrogen) (Water)
The second catalyst 24 is the catalyst of an organic acid group for a removal of the bed smell, and its chemical expression is as follows;
CmHn + 02 → CO* + H_. O
( sl-' -fc) ( £) 350tI4-H (o]A s}εV.ά ) ( )
(Hydrocarbon) (Oxygen) 350°C catalyst (Carbon dioxide) (Water)
The third catalyst 25 is the catalyst for a removal of carbon monoxide and VOC's, and its chemical expression is as follows;
(HO + 02 → COa + H8 O sB^) 35QT %τ1 (°]A>3 >4I) ( -)
(Hydrocarbon) 350°C catalyst (Carbon dioxide) (Water)
The fourth catalyst 26 is the catalyst for use in removing a volatile organic chemical compound, and its chemical expression is as follows;
(se πH ^pJ) (U4ι) 350t p]| (o] isl- ^) Mr) C4 )
(Trimethylamine) (Oxygen) 350°C catalyst (Carbon dioxide) (Water)
(Nitrogen)
The fifth catalyst 27 is the catalyst for a removal of dioxin, and its chemical expression is as follows;
250 - 3501C
)3^ SX 4 0ι ~ C02 r 11*0 +C12
Cl O Cl
(PCDD)
2,3,7,8 Tetra chloro dibenzo dioxin Oxygen Catalyst Carbon dioxide Water Chlorine (Dioxin) (Oxygen) Carbon Dioxide(Carbonic gas)
Organic matter difficult in decomposition
I ) y > z SJ 3 ?
CxHyClz + (x+0.2y-0.25z)Oa → x002 + (0.5y - Q.5z)Hj.O + zHCI
II ) y < z SI ^
CxHyCiz + (x+0.2y-0.25z)O2 + (0.5y - 0.5z)H2O → xC02 + zHCI
Case of y > z Case ofy < z
The air tank 3 is to cool carbonated gas transferred through a series of the catalysts, the first through fifth catalysts, into temperature approximate to room temperature. Such an air tank 3 has an airtight receptacle structure in which a plurality of gas convection preventing plates 31 are provided with a constant capacity. On one side of the air tank 3, an inflow opening 32 is formed through a pipe connection. On one side of the inflow opening 32, a discharge opening 33 is formed through a pipe connection.
Herewith, the discharge opening 33 of the air tank 3 has a seat type activated carbon 321 and an ion filter 331 in the inside thereof, as shown in Fig. 1. The auxiliary filtering device 4 secondarily filters the carbonated gas transferred through the air tank 3. Such an auxiliary filtering device 4 is preferably constructed by sequentially arraying a basic activated carbon 41, an acid activated carbon 42 and a neutral activated carbon 43 in the inside thereof, as shown in Fig. 1. In the ozone generator 5, between corresponding electrodes as shown in the following chemical reaction expression, it is used a general ozone generator in which electron generated by applying AC(alternate current) voltage of high voltage,
25,000 V ~ 30,000 V, to the front of one electrode through a use of a glass dielectric body, reacts to an oxygen molecule O2 to thus generate ozone (O3). Such an ozone generator is preferably limited to 0.03ppm ~ 0.05ppm in an ozone
generation quantity in the present invention.
(Chemical Reaction Expression of Ozone)
02 + c - → O + O + e -■
02 + e - → Oa + c -
O + 02 --> Os
Oz + 02 → Os + O
The vacuum pump 6 is a kind of carbonated gas exhausting units for pressurizing the carbonated gas transferred through the auxiliary filtering device 4 by a constant pressure and for transferring it to the water tank 7. One side face of the vacuum pump 6 is preferably connected to an air generation pipe 61 having numerous air generation holes P as shown in Fig. 1.
The water tank 7 finally filters the carbonated gas flowing in through the vacuum pump 6, and exhausts it in air. Such a water tank 7 is formed by filling up a receptacle inside of a constant quantity with water. One side upper part of the water tank is provided with a gas exhaust opening 71.
While, the electron control panel device 8 automatically controls a series of constructive parts described above, so as to control a series of driving relations required for a carbonizing operation, such as temperature and time of a far infrared rays heater, temperature of respective catalysts, and other driving relations, etc.
Preferably, the electron control panel device 8 as the automatic control unit is formed as a general electron control device having a circuit connection relation as shown in Fig. 2.
Therefore, with such a described construction, and in a mutual combination with the carbonizing apparatus using the far infrared rays heater, as shown in Fig. 1, the far infrared rays heater 11 and the carbonizing receptacle 12 are installed inside the body case 1, and the body case 1 is formed in one body with the catalyst insulation 2 in structure connected through an upper center portion of the body case 1. That is, as shown in Fig. 1, the air tank 3, the auxiliary filtering device 4 and the vacuum pump 6 are connected with one another in a serially piped connection structure. Under such a connection construction, the ozone generator 5 as a separate construction is installed on one side of the vacuum pump 6. The ozone generator 5 is coupled with the vacuum pump 6. Further, the air generation pipe 61 of the vacuum pump 6 is structured to be inserted into the water tank 7. Such a serial construction embodies the inventive carbonizing apparatus using the far infrared rays heater.
Operations of the carbonizing apparatus using the far infrared rays heater will be described as follows.
First, the carbonizing receptacle 12 installed inside the case body 1 is filled with waste matter 10. Under such a state, when initial power is supplied by using the electron control panel device 8 shown in Fig. 2, the far infrared rays heater 11 installed inside the case body 1 emits radiant heat of high temperature, and heats the carbonizing receptacle 12 to start to progress the carbonizing operation.
Such a far infrared rays heater 11 has a line connection structure closely
arrayed on the bottom face of the carbonizing receptacle 12, and the line closely, arrayed on the bottom face of the carbonizing receptacle 12 is inserted and installed into the inside of the carbonizing receptacle 12 through an upper part face of the carbonizing receptacle 12. According to such a structure, direct heat of a range of 350~400°C is applied onto the waste matter filled into the carbonizing receptacle 12. At this time, the carbonizing receptacle 12 with ceramic urethane coating process operates so that carbonated material may not get scorched thereto.
The insulation brick 13 as an inner wall face of the case body 1 is made of oxide aluminum, alumina and ocher, and has an insulation effect enduring against a temperature range of 1200~1300°C. The insulation brick 13 also has a function of partially suctioning vapor generated in the carbonizing operation, and simultaneously evaporates and removes the suctioned vapor by using carbonizing heat.
On the other hand, in case that waste matter is carbonized through the far infrared rays heater 11 and the carbonizing receptacle 12, noxious carbonated gas is generated inside the body case 1, and such a generated carbonated gas is passed through a primary dehumidifying procedure of the dehumidifier 21, and then flows into the catalyst insulation 2.
Subsequently, the catalyst insulation 2 turns power on at 350°C of the carbonated gas that flows thereinto through a temperature sense of the catalyst automatic temperature sensor 28, and heats the catalyst heater 22 and the catalyst alien substance removal heater 29. Interior temperature of a series of catalysts, the first through fifth catalysts, as an accumulated structure, is maintained in a temperature range of 250 ~350°C by such a heating operation, and primarily filters
the pollution material of the carbonated gas through the catalysts 23, 24, 25, 26, 27. At this time, the catalyst alien substance removal heater 29 has a self cleaning function, and operates for about 2 hours in a temperature range of 500 ~550°C, one time every a constant period based on a carbonizing operation, about three months, so as to selectively remove alien substances remained inside the first through fifth catalysts. While such a catalyst alien substances removal heater 29 operates, it is desirable not to progress a specific carbonizing operation.
Next, the carbonated gas passed through the catalyst insulation 2 inflows into the air tank 3 along a piped line. According that the carbonated gas flows into the air tank 3, the gas convection preventing plate 31 disposed inside the air tank 3 delays a staying time of the fiown-in carbonated gas so as to cool temperature of the carbonated gas into temperature approximate to room temperature.
The carbonated gas passed through the air tank 3 flows into the auxiliary filtering device 4 through a piped line. In the auxiliary filtering device 4, trimethylamine, monomethylamine and ammonia etc. are removed from the carbonated gas through the basic activated carbon 41. Benzene, toluene, xylan, styrene, carbon bisulfide, acetic acid, bodice acetic acid, lactic acid, hydrogen sulfide, methylmercaptan, and dimethylsulfide, etc., which are contained into the carbonated gas, are eliminated through the acid activated carbon 42. Ethanol, acetic acid, bodice acetic acid, lactic acid, formicaldehyde, acetaldehyde, ethylene, and carbon monoxide, etc., which are contained into the carbonated gas, are removed through the neutral activated carbon 43.
The carbonated gas from which the harmful material is removed through the auxiliary filtering device 4, flows into the inside of the vacuum pump 6. Under
such a state that the carbonated gas is mixed with ion gotten from the ion generator 5, the gas is transferred to the inside of the water tank 7 through the air generation pipe 61. Then, the carbonated gas is finally filtered through water filled into the water tank 7, and exhausted to the air through the gas exhaust opening 71. Thereby, all of carbomzing operations are completed.
When all the carbonizing operation were completed, the cooling fan 14 and the blast suction opening 15 formed on the case body 1 are automatically driven by the electron control panel device 8, to compulsively ventilate and cool a heat source of the case body 1 inside heated through the carbonizing operation. When temperature of the carbonizing receptacle inside the case body 1 falls to
75 ~ 80°C by such a cooling operation, a buzzer rings by a temperature sense of the carbonizing temperature sensor (not shown in the drawings).
Like this, when the buzzer rings to inform a worker of a completion of the carbonizing operation, the worker opens the door D of the body case 1 as shown in Fig. 2. Under such an opening state of the door, the carbonizing receptacle 12 that fallen in temperature, is taken out of the body case inside, to the outside. The carbonizing matter 10 is finally processed as waste matter.
INDUSTRIAL APPLICABILITY As afore-mentioned, in accordance with the present invention, a carbonizing apparatus using a far infrared rays heater can extremely heighten an operation efficiency by shortening a temperature rise time necessary for a carbonizing operation through a direct heating method using a cartridge heater of far infrared rays, and thus by preventing an unnecessary loss of power.
In addition, a carbonizing apparatus using a far infrared rays heater can prevent a serious air pollution, by rapid cooling a carbonizing receptacle through a heat cooling device so as to easily discharge carbonized matter, and simultaneously, by effectively removing various kinds of noxious gases and a bed smell generated in the midst of a carbonizing operation through a filtering unit having multi filtering steps.
It will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without deviating from the spirit or scope of the invention. Thus, it is intended that the present invention cover the modifications and variations of this invention provided they come within the scope . of the appended claims and their equivalents.