JP2000159924A - Apparatus for recovering organic substance - Google Patents

Abstract

PROBLEM TO BE SOLVED: To recover an organic substance as a solidified substance fuel or a liquefied substance fuel by equipping an organic substance recovering apparatus with an organic gas treating mechanism part and an organic substance recovering part, capable of decomposing a waste plastic material, improving the flow of an organic gas and stirring/cooling the organic gas. SOLUTION: An organic gas G is supplied to an organic gas inlet pipe 4 and heated to 130-350 deg.C by a heating medium from a heating medium guide pipe 6 to prevent liquefaction and solidification. The organic gas G heated to a high temperature by the heating medium is cooled by a cold medium from a cooking medium guide pipe 7 while being stirred by a stirring force of a stirring mechanism part 8 driven by the driving force of a motor 9 and separated into a liquefied substance, a solidified material and a hydrogen chloride gas. The liquefied substance and the solidified substance flow along the wall face of a barrel 3 and the surface of the stirring mechanism part 8 and recovered in an organic substance recovery tank 10. The liquefied substance and the solidified substance are collected through an organic substance transporting mechanism part 11, a hopper 12 and a valve 13 in an organic substance storage tank 14 and supplied as a fuel from it.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0001]

BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an organic substance recovery apparatus for effectively removing organic substances contained in a gas generated during a dehydrochlorination treatment of a waste plastic material.

[0002]

2. Description of the Related Art In recent years, in the field of industrial waste, the shortage of waste disposal sites and the legal regulations have made it impossible to freely dump waste into disposal sites. The effective utilization of resources is being changed by changing to solid fuel or oil fuel.

[0003] Since the waste plastic material contains vinyl chloride (hereinafter referred to as PVC) as a main component, harmful gases such as hydrogen chloride are generated when the fuel is used. For this reason, when converting waste plastic material into fuel, dehydrochlorination treatment is performed.

[0004] When PVC is subjected to dehydrochlorination treatment, PV
The gas generated from C includes not only hydrogen chloride gas but also organic substances such as phthalic anhydride, higher alcohols contained in the plasticizer, and hydrocarbons generated during decomposition of PVC. I have. When these organic substances are recovered as solidified fuel or oily fuel, the organic gas generated during the processing may adhere to pipes and local parts of equipment, deteriorating the gas flow and reducing the processing capacity.

[0005] Recently, for example, Japanese Patent Application Laid-Open No. 8-92567 discloses a technique for decomposing a waste plastic material and improving the flow rate of organic gas generated during the decomposition to improve the recovery rate.

[0006]

Problems to be Solved by the Invention Japanese Patent Application Laid-open No. Hei 8-92567
In the technology described in Japanese Patent Laid-Open Publication No. H10-260, when phthalic anhydride generated during decomposition of waste plastic material is solidified and recovered, a cooler is used, and high-temperature organic gas is cooled to 130 ° C. by the cooler.
It has been cooled to about the temperature.

However, the organic gas contains higher alcohols in addition to phthalic anhydride as described above.
In particular, phthalic anhydride solidifies at a temperature of about 130 ° C., while other organic gases, such as higher alcohols, form about 1%.
It is known to liquefy below a temperature of 00 ° C. For this reason, if the cooling temperature of the organic gas is set to about 130 ° C. as in Japanese Patent Application Laid-Open No. 8-92567, other organic gases flow to the next processing unit without being liquefied, and There was a problem or inconvenience that could not be properly collected.

The present invention has been made in view of such circumstances, and has been made to improve the flow of the organic gas generated during the decomposition of the waste plastic material, and to make all of the organic gas at a temperature of 100 ° C.
It is an object of the present invention to provide an organic matter recovery apparatus that can be appropriately solidified or liquefied even below and can be recovered as fuel.

[0009]

According to a first aspect of the present invention, there is provided an organic matter recovery apparatus comprising an organic gas processing mechanism and an organic matter recovery unit. In the apparatus, an organic gas heating means provided on the entrance side of the body of the organic gas processing mechanism, a stirring mechanism accommodated in the body and stirring the heated organic gas, and stirring the organic gas by the stirring mechanism Inside, provided on the outside of the body, an organic gas cooling means for generating a solidified product or a liquefied product by stirring the organic gas at a low temperature, and being separated from the organic gas during the stirring and cooling of the organic gas. And a means for discharging the hydrogen chloride gas, wherein one of a solidified product and a liquefied product generated during stirring and cooling of the organic gas is recovered in the organic material recovery section.

[0010] In order to achieve the above object, an organic matter recovery apparatus according to the present invention has the following features.
The organic gas heating means is constituted by a heating medium guide tube surrounding the organic gas inlet of the body.

[0011] In order to achieve the above object, an organic matter recovery apparatus according to the present invention has the following features.
A motor is provided in the stirring mechanism.

Further, in order to achieve the above object, the organic matter recovery apparatus according to the present invention has the following features.
The stirring mechanism is constituted by an intermeshing screw in which blades are fixed to a plurality of drive shafts.

In order to achieve the above object, an organic matter recovery apparatus according to the present invention has the following features.
The stirring mechanism is characterized by comprising a meandering rotor and a universal joint interposed on a drive shaft connecting the rotor and the motor.

Further, in order to achieve the above object, the organic matter recovery apparatus according to the present invention has the following features.
A peak portion and a valley portion are continuously formed on the body accommodating the meandering rotor as the stirring mechanism, in accordance with the shape of the meandering rotor.

Further, in order to achieve the above object, an organic matter recovery apparatus according to the present invention has the following features.
The stirring mechanism is characterized by comprising a drive shaft connected to the motor and a scraping rod fixed to the drive shaft.

Further, in order to achieve the above object, an organic matter recovery apparatus according to the present invention has the following features.
The stirring mechanism is characterized by comprising a stirring plate fixed to a drive shaft connected to a motor, and a ball housed in the body and rotated by the rotating force of the stirring plate.

Further, in order to achieve the above object, the organic matter recovery apparatus according to the present invention has the following features.
The agitation mechanism is formed as a meshing screw part having blades fixed to a plurality of drive shafts, and a partition for reversing a cooling medium flowing inside the drive shaft is provided.

According to a tenth aspect of the present invention, there is provided an organic matter recovery apparatus according to the present invention, wherein the organic gas cooling means surrounds the outside of the body along the axial direction of the body. It is characterized by comprising a medium guide tube.

Further, in order to achieve the above object, the organic matter recovery apparatus according to the present invention is characterized in that the hydrogen chloride gas discharge means is provided with an oil droplet recovery section.

Further, in order to achieve the above object, the organic substance recovery apparatus according to the present invention comprises an organic substance recovery section, which comprises: One of the liquefied materials is constituted by an organic matter recovery tank for temporarily collecting the collected matter and an organic matter transfer mechanism for supplying one of the collected solidified matter and the liquefied matter to the organic matter storage tank.

According to a third aspect of the present invention, there is provided an organic matter recovery apparatus including an organic gas processing mechanism and an organic matter recovery section. An organic gas heating means provided on the entrance side of the body of the organic gas processing mechanism, a stirring mechanism accommodated in the body and stirring the heated organic gas, and the body being stirred by the stirring mechanism while the organic gas is being stirred. An organic gas cooling means that is provided on the outside and generates one of a solidified product and a liquefied product by stirring the organic gas at a low temperature,
During the stirring and cooling of the organic gas, a means for discharging the hydrogen chloride gas separated from the organic gas, a pressure of the organic gas flowing through the inlet of the body and a pressure of the hydrogen chloride gas flowing through the means for discharging the hydrogen chloride gas are used. A control operation unit for detecting and detecting a pressure difference between the gases and applying a driving force to the stirring mechanism unit when the difference is calculated, wherein a solidified substance and a liquefied substance generated during stirring and cooling of the organic gas are provided. One of the materials is collected in the organic material collecting section.

[0022]

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of an organic matter recovery apparatus according to the present invention will be described below with reference to the drawings.

FIG. 1 is a schematic view showing a first embodiment of the organic matter recovery apparatus according to the present invention.

The organic matter recovery apparatus according to the present embodiment includes an organic gas processing mechanism 1 for liquefying or solidifying an organic gas, and an organic matter recovery unit 2 for collecting liquefied or solidified organic matter.

The organic gas processing mechanism 1 supplies an organic gas inlet pipe 4 for guiding the organic gas G to the cylindrical body 3 and hydrogen chloride gas generated when the organic gas G is liquefied or solidified to other equipment. A hydrogen chloride gas discharge pipe 5 is provided.

The organic gas processing mechanism 1 has a double cylinder formed on the outside of the organic gas inlet pipe 4 along the axial direction.
A heating medium guide tube 6 for guiding the heating medium is provided, and a cooling medium guide tube 7 for forming a double cylinder on the outside of the body 3 along the axial direction and guiding the cooling medium is provided.

The organic gas processing mechanism 1 includes a stirring mechanism 8 having, for example, blades, housed in the body 3, and a motor 9 for driving the stirring mechanism 8.

On the other hand, the organic substance recovery section 2 comprises an organic substance recovery tank 10 for recovering organic substances liquefied or solidified by the organic gas processing mechanism section 8, and an organic substance transfer mechanism section 11, a hopper 12 and a valve 13. An organic matter storage tank 14 is provided for storing the waste matter.

Next, the operation will be described.

In the organic matter recovery apparatus according to the present embodiment, when the organic gas is liquefied or solidified into a fuel, heating and cooling of the organic gas are performed.

An organic gas G which is generated during the dehydrochlorination process and contains hydrogen chloride as a main component and contains phthalic anhydride, higher alcohols, and fats and oils is supplied to the organic gas inlet pipe 4.
At that time, the organic gas G is heated at 130 ° C. to 350 ° C. by the heating medium from the heating medium guide tube 6 to prevent liquefaction or solidification. In particular, the connecting portion between the heating medium guide tube 6 and the body 3 is a portion to which the stirring force of the stirring mechanism 8 does not reach, and the organic gas G is deposited and deposited so that the flow does not deteriorate. Heating at the above-mentioned temperature.

As the organic gas G heated by the heating medium from the heating medium guide tube 6 flows toward the center of the body 3, the organic gas G of the stirring mechanism 8 driven by the continuous or intermittent driving force of the motor 9. While being stirred by the stirring force, the cooling medium guide pipe 7 is used to cool with a cooling medium, and at the time of cooling, is separated into a liquefied or solidified substance and hydrogen chloride gas. The cooling temperature has an appropriate value depending on the type of the substance contained in the organic gas G. In the case of phthalic anhydride, the cooling temperature is preferably 100 ° C. or less, and in the case of higher alcohols and fats and oils, 6 ° C.
0 ° C. or less is appropriate.

The liquefied matter or solidified matter generated from the organic gas G flows along the wall surface of the body 3 or the surface of the stirring mechanism 8 and is collected in the organic matter recovery tank 10. Further, the hydrogen chloride gas separated from the organic gas G is processed again by another device through the hydrogen chloride gas discharge pipe 5.

The liquefied matter or solidified matter collected in the organic matter recovery tank 10 is collected in an organic matter storage tank 14 via an organic matter transfer mechanism 11, a hopper 12, and a valve 13, and is supplied to a demand destination as fuel therefrom. .

As described above, in the present embodiment, the portion of the stirring mechanism 8 to which the stirring force does not reach is heated by the heating medium to the organic gas G, thereby preventing the organic gas G from adhering to and accumulating on the body 3. When the flow of the gas G was improved and the heated organic gas G was stirred by the stirring mechanism 8, the organic gas G was cooled or cooled to a temperature of 100 ° C. or less to liquefy or solidify the organic gas G.
Can be further promoted into a liquefied or solidified product, and the organic gas G can be recovered by separating the liquefied or solidified product and the hydrogen chloride gas from the organic gas G well.

FIG. 2 is a schematic view showing a second embodiment of the organic matter recovery apparatus according to the present invention. The same components as those of the first embodiment are denoted by the same reference numerals.

The organic matter recovery apparatus according to the present embodiment has a first
Stirring mechanism 8 of organic gas processing mechanism 1 shown in the embodiment
And the meshing screw portion 15 is adopted.
That is, the organic gas processing mechanism unit 1 supplies the organic gas inlet pipe 4 for guiding the organic gas G to the cylindrical body 3 and the hydrogen chloride gas generated when the organic gas G is liquefied or solidified to other devices. A hydrogen chloride gas discharge pipe 5 is provided.

The organic gas processing mechanism 1 has a double cylinder formed on the outside of the organic gas inlet pipe 4 along the axial direction.
A heating medium guide tube 6 for guiding the heating medium is provided, and a cooling medium guide tube 7 for forming a double cylinder on the outside of the body 3 along the axial direction and guiding the cooling medium is provided.

On the other hand, the stirring mechanism section 8 of the organic gas processing mechanism section 1 is configured by housing the meshing screw section 15 in the body 3. The meshing screw portion 15 includes a first drive shaft 16 and a second drive shaft 17. Blades 18 and 19 are fixed to each drive shaft 16 and 17, and each drive shaft 1
6 and 17 are screwed together via gears 20 and 21 and the motor 9
With the driving force described above, the rotation directions of the blade 18 of the first drive shaft 16 and the blade 19 of the second drive shaft 17 are made different from each other via the gears 20 and 21 to stir the organic gas G. In the present embodiment, the meshing screw portion 15 housed in the body 3 is of a biaxial type, but this is merely an example, and may be a triaxial type or more.

In the organic gas processing mechanism 1 having such a structure, hydrogen chloride is used as a main component, phthalic anhydride,
As in the first embodiment, the organic gas G containing higher alcohols and fats and oils is heated by the heating medium from the heating medium guide tube 6 and, as it flows toward the body 3, continuously or continuously by the meshing screw portion 15. It is intermittently stirred, and is cooled by the cooling medium from the cooling medium guide tube 7 at that time.
It is formed into a liquefied or solidified product. Hydrogen chloride gas generated during the generation of a liquefied or solidified organic gas G is supplied to another device through a hydrogen chloride gas discharge pipe 5. Also,
The liquefied matter or solidified matter is collected in an organic matter recovery tank 10 provided at the bottom of the body 3.

According to the present embodiment, the meshing type in which the first drive shaft 16 having the blade 18 fixed thereto and the second drive shaft 17 having the blade 19 fixed thereto as the stirring mechanism 8 in the body 3 is combined. Since the screw portion 15 is accommodated and the organic gas G being cooled is stirred by the stirring force of the meshing screw portion 15, the organic gas G can be surely formed into a liquefied material or a solidified product and collected.

FIG. 3 is a schematic view showing a third embodiment of the organic matter recovery apparatus according to the present invention. The same components as those of the first embodiment are denoted by the same reference numerals.

The organic matter recovery apparatus according to the present embodiment comprises a first
Stirring mechanism 8 of organic gas processing mechanism 1 shown in the embodiment
The rotor 22 is employed as a rotor, and the rotor 22 is formed in a meandering shape.

The meandering rotor 22 includes universal joints 23 and 24, a rod 25, and a drive shaft 26.
Is connected to the motor 9. Further, the body 3 accommodating the meandering rotor 22 has a rotor 22 therein.
And a stator portion 29 for continuously forming a peak portion 27 and a valley portion 28 in conformity with the shape of.

As described above, in the present embodiment, the stirring mechanism 8
The meandering rotor 22 is used as the universal joints 23 and 24 and the rod 2
5, connected to the motor 9 with the drive shaft 26 interposed,
Is provided with a stator portion 29 in which peaks 27 and valleys 28 are alternately and continuously formed, and the organic gas G guided from the organic gas inlet pipe 4 is heated by the heating medium from the heating medium guide pipe 6. After that, the meandering rotor 22 is rotated by the continuous or intermittent driving force from the motor 9 to apply a pressing force to the organic gas G flowing in the gap between the rotor 22 and the stator portion 29, and during this time, the cooling medium guide pipe The organic gas G is cooled by the cooling medium from Step 7 to produce a liquefied substance or a solidified substance from the organic gas G and separate the hydrogen chloride gas.

The hydrogen chloride gas separated from the organic gas G is supplied to another device through a hydrogen chloride gas discharge pipe 5. In addition, a liquefied substance or a solidified substance generated from the organic gas G is collected in the organic substance recovery tank 10.

As described above, in the present embodiment, the meandering rotor 22 is employed as the stirring mechanism 8 and the pressing force applied to the organic gas G from the meandering rotor 22 is increased. Formation into a solid or a solid can be further promoted.

FIG. 4 is a schematic view showing a fourth embodiment of the organic matter recovery apparatus according to the present invention. The same components as those of the first embodiment are denoted by the same reference numerals.

The organic matter recovery apparatus according to the present embodiment has a first
Stirring mechanism 8 of organic gas processing mechanism 1 shown in the embodiment
As shown in FIG. 5, a flat scraping rod 31 is provided on a drive shaft 30 which is driven continuously or intermittently by the driving force of a motor 9, and a projection 32 is provided inside the body 3 as shown in FIG. It is a thing.

As described above, in the present embodiment, the stirring mechanism 8
A scraping rod 31 is provided on the drive shaft 30, and a projection 32 is provided on the body 3, and the scraping rod 31 is swung by the driving force of the motor 9, and the organic gas G flowing in the body 3 is projected on the projection 32. Because of the collision and agitation, the adhesion and deposition of the organic gas G on the body 3 can be reduced and the flow of the organic gas G can be improved, and the generation of the organic gas G into a liquefied substance or a solidified substance can be promoted. Can be done.

FIG. 6 is a schematic view showing a fifth embodiment of the organic matter recovery apparatus according to the present invention. The same components as those of the first embodiment are denoted by the same reference numerals.

The organic matter recovery apparatus according to the present embodiment comprises a first
Stirring mechanism 8 of organic gas processing mechanism 1 shown in the embodiment
A flat stirring plate 34 is provided on a drive shaft 33 that is driven continuously or intermittently by the driving force of a motor 9, and a small spherical ball 35 is filled in the body 3. In addition, in the organic matter recovery tank 10 provided at the bottom of the body 3, a vent plate 36 for preventing the outflow of the balls 35 is provided.
The surface of the ball 35 has a function of a filter.

As described above, in the present embodiment, the stirring mechanism 8
A stirring plate 34 fixed to the drive shaft 33 and a ball 35 to be filled in the body 3 are provided, and the stirring plate 34 is rotated by the driving force given by the motor 9.
5, the organic gas G was made to adhere to the ball 35, so that the flow of the organic gas can be improved and the formation of a liquefied substance or a solidified substance can be promoted.

FIG. 7 is a schematic view showing a sixth embodiment of the organic matter recovery apparatus according to the present invention. The same parts as those of the second embodiment are denoted by the same reference numerals.

The organic matter recovery apparatus according to the present embodiment has a second
Stirring mechanism 8 of organic gas processing mechanism 1 shown in the embodiment
The first drive shaft 16 of the meshing screw portion 15 provided as
Cooling medium inlets 16a, 17a and cooling medium outlets 16b, 1 for supplying and discharging a cooling medium to and from the second drive shaft 17, respectively.
7b, and partitions 16c, 17c in which the cooling medium flows in a U-turn to flow inside the first drive shaft 16 and the second drive shaft 17, respectively.

As described above, in the present embodiment, the cooling medium is caused to flow through each of the first drive shaft 16 and the second drive shaft 17 of the meshing screw portion 15 to cool the stirring organic gas. The solidification or liquefaction of the organic gas can be further promoted in combination with the cooling medium from the medium guide pipe 7, and the thermal stress of each of the first drive shaft 16 and the second drive shaft 17 generated during stirring can be suppressed to a low level. High strength can be maintained.

FIG. 8 is a schematic view showing a seventh embodiment of the organic matter recovery apparatus according to the present invention. The same components as those of the first embodiment are denoted by the same reference numerals.

The organic matter recovery apparatus according to the present embodiment comprises a first
A pressure gauge 3 is provided on each of the organic gas inlet pipe 4 and the hydrogen chloride gas discharge pipe 5 of the organic gas processing mechanism 1 shown in the embodiment.
7 and 38 are provided. When the pressure exceeds a predetermined set pressure between the pressure of the organic gas G detected by the pressure gauge 37 and the pressure of the hydrogen chloride gas detected by the pressure gauge 38, the motor 9 is used. Control operation section 39 for driving the stirring mechanism section 8
Is provided.

As described above, in the present embodiment, the pressure gauge 3 is provided on each of the organic gas inlet pipe 4 and the hydrogen chloride gas discharge pipe 5.
7 and 38 are provided, and a control operation section 39 performs an operation based on each signal detected from each of the pressure gauges 37 and 38. If a deviation occurs in the operation, the deviation exceeds a predetermined set value. At this time, the motor 9 is driven by an operation signal from the control operation unit 39 that recognizes that the organic gas G is attached and deposited on the body 3, and the stirring mechanism 8 is driven based on the operation signal, thereby adhering to the body 3. -The organic gas G to be deposited is removed.

Therefore, according to the present embodiment, during the cooling of the organic gas G flowing in the body 3 by the cooling medium from the cooling medium guide tube 7, the organic gas G adheres and accumulates on the body 3 and , 38 exceeds a predetermined set pressure value, a control operation section 39 for rotating and driving the stirring mechanism section 8 based on the operation signal is provided, so that the flow of the organic gas G is improved. To promote formation into a liquefied or solidified product.

FIG. 9 is a schematic view showing an eighth embodiment of the organic matter recovery apparatus according to the present invention. The same components as those of the first embodiment are denoted by the same reference numerals.

The organic matter recovery apparatus according to the present embodiment comprises a first
An oil / fat recovery unit 40 is provided in the hydrogen chloride gas discharge pipe 5 of the organic gas processing mechanism unit 1 shown in the embodiment, and when the organic gas G is liquefied or solidified, it flows through the body 3 with the cooling medium from the cooling medium guide pipe 7. The oils and fats not removed from the organic gas G during the cooling of the organic gas G are removed.

As described above, in the present embodiment, the oil / fat recovery unit 40 is provided in the hydrogen chloride gas discharge pipe 5 to collect the oil / fat not removed from the organic gas G during the cooling of the organic gas G flowing in the body 3. Since the hydrogen chloride gas is removed by the unit 40, the hydrogen chloride gas can be satisfactorily processed when the hydrogen chloride gas is supplied to another device.

[0064]

As described above, the organic matter recovery apparatus according to the present invention comprises a means for heating an organic gas containing hydrogen chloride as a main component, which is generated during a dehydrochlorination treatment process of a waste plastic material; While the agitation mechanism for agitating the subsequent organic gas and the means for cooling the organic gas agitated by the agitation mechanism are incorporated in the organic gas processing mechanism, the solidified material generated from the organic gas in the organic gas processing mechanism or Equipped with an organic matter recovery section for recovering liquefied matter, heating the organic gas by heating means to improve its flow, and cooling the organic gas to a temperature of 100 ° C. or less while cooling the organic gas while stirring the organic gas. Since the solidified product or the liquefied product is generated, the organic gas can be reliably converted into the solidified product or the liquefied product, and the waste plastic material can be effectively recovered.

[Brief description of the drawings]

FIG. 1 is a schematic view showing a first embodiment of an organic matter recovery apparatus according to the present invention.

FIG. 2 is a schematic diagram showing a second embodiment of the organic matter recovery apparatus according to the present invention.

FIG. 3 is a schematic view showing a third embodiment of the organic matter recovery apparatus according to the present invention.

FIG. 4 is a schematic view showing a fourth embodiment of the organic matter recovery apparatus according to the present invention.

FIG. 5 is a sectional view taken along the line AA of FIG. 4;

FIG. 6 is a schematic view showing a fifth embodiment of the organic matter recovery apparatus according to the present invention.

FIG. 7 is a schematic view showing a sixth embodiment of the organic matter recovery apparatus according to the present invention.

FIG. 8 is a schematic view showing a seventh embodiment of the organic matter recovery apparatus according to the present invention.

FIG. 9 is a schematic diagram showing an eighth embodiment of the organic matter recovery apparatus according to the present invention.

[Explanation of symbols]

 DESCRIPTION OF SYMBOLS 1 Organic gas processing mechanism part 2 Organic substance recovery part 3 Body 4 Organic gas inlet part 5 Hydrogen chloride gas discharge pipe 6 Heating medium guide pipe 7 Cooling medium guide pipe 8 Stirring mechanism part 9 Motor 10 Organic substance recovery tank 11 Organic substance transfer mechanism part 12 Hopper DESCRIPTION OF SYMBOLS 13 Valve 14 Organic matter storage tank 15 Mesh screw part 16 1st drive shaft 16a Coolant inlet 16b Coolant outlet 16c Partition 17 2nd drive shaft 17a Coolant inlet 17b Coolant outlet 17c Partition 18 Blade 19 Blade 20 Gear 21 Gear 22 Rotor 23 Universal joint 24 Universal joint 25 Rod 26 Drive shaft 27 Crest portion 28 Valley portion 29 Stator portion 30 Drive shaft 31 Scraping rod 32 Projection 33 Drive shaft 34 Stir plate 35 Ball 36 Opening plate 37 Pressure gauge 38 Pressure gauge 39 System Calculation unit 40 the oil droplet recovery unit

 ──────────────────────────────────────────────────続 き Continuing from the front page (72) Inventor Hironori Abe 1-1-1, Shibaura, Minato-ku, Tokyo F-term in Toshiba head office (reference) 4D004 AA07 AA08 AB05 AB06 AB10 BA03 BA06 CA22 CA25 CA32 CA45 CB21 4D076 AA01 AA13 AA15 AA16 AA22 BC04 BC06 BE04 BE06 CB05 CD12 CD16 DA02 DA21 EA02Y EA05Y EA12Y HA03 HA20 JA01 JA04 4F301 AA17 AB01 AB03 CA07 CA24 CA26 CA43 CA62 CA63 CA72 CA73 4H015 AA02 CA01 BB01 CB03

Claims (13)

[Claims] 1. An organic material recovery device comprising an organic gas processing mechanism and an organic material recovery unit, wherein an organic gas heating means provided on an inlet side of a body of the organic gas processing mechanism, and a heating unit accommodated in the body, A stirring mechanism for stirring the organic gas, and a stirring mechanism for stirring the organic gas, which is provided on the outside of the body to stir the organic gas at a low temperature to produce either a solidified product or a liquefied product. An organic gas cooling means, and a means for discharging hydrogen chloride gas separated from the organic gas during stirring / cooling of the organic gas, wherein any of solidified and liquefied substances generated during stirring / cooling of the organic gas is provided. An organic matter recovery apparatus, wherein one of the organic matter recovery sections is collected by the organic matter recovery section. 2. The organic matter recovery apparatus according to claim 1, wherein the organic gas heating means is constituted by a heating medium guide tube surrounding the organic gas inlet of the body. 3. The organic matter recovery apparatus according to claim 1, wherein a motor is provided in the stirring mechanism. 4. The organic matter recovery apparatus according to claim 1, wherein the stirring mechanism comprises a meshing screw unit having a plurality of drive shafts fixedly provided with blades. 5. The stirrer according to claim 1, wherein the stirring mechanism comprises a meandering rotor and a universal joint interposed on a drive shaft connecting the rotor and the motor. An organic matter recovery device as described in the above. 6. A body for accommodating a meandering rotor as a stirring mechanism portion, wherein peaks and valleys are continuously formed in accordance with the shape of the meandering rotor. Item 6. An organic matter recovery apparatus according to Item 5. 7. The organic matter recovery apparatus according to claim 1, wherein the stirring mechanism includes a drive shaft connected to the motor, and a scraping rod fixed to the drive shaft. 8. A stirrer comprising a stirrer plate fixedly mounted on a drive shaft connected to a motor, and a ball housed in the body and rotated by the rotational force of the stirrer plate. 4. The organic matter recovery device according to 1 or 3. 9. The stirrer according to claim 6, wherein the stirring mechanism is formed as a meshing screw having a plurality of drive shafts with blades fixed thereto, and a partition for reversing a cooling medium flowing inside the drive shaft is provided. The organic matter recovery apparatus according to claim 1. 10. The organic matter recovery apparatus according to claim 1, wherein the organic gas cooling means is constituted by a cooling medium guide tube which surrounds the outside along the axial direction of the body. 11. The organic matter recovery apparatus according to claim 1, wherein an oil droplet recovery unit is provided in the hydrogen chloride gas discharge means. 12. An organic matter recovery section, an organic matter recovery tank for temporarily collecting either solidified or liquefied organic gas generated from the organic matter processing mechanism, or one of the collected solidified or liquefied matter. 2. The organic matter recovery apparatus according to claim 1, wherein one of the organic matter recovery mechanisms includes an organic matter transfer mechanism for supplying the organic matter to the organic matter storage tank. 13. An organic matter recovery apparatus provided with an organic gas processing mechanism and an organic matter recovery unit, wherein an organic gas heating means provided on an inlet side of a body of the organic gas processing mechanism, and a heating unit accommodated in the body, A stirring mechanism for stirring the organic gas, and a stirring mechanism for stirring the organic gas, which is provided on the outside of the body to stir the organic gas at a low temperature to produce either a solidified product or a liquefied product. Organic gas cooling means, means for discharging hydrogen chloride gas separated from the organic gas during stirring and cooling of the organic gas, and means for discharging the pressure of the organic gas flowing through the inlet of the body and the hydrogen chloride gas. A control operation unit for detecting the pressure of the flowing hydrogen chloride gas, calculating a deviation when a pressure difference occurs between the respective gases, and applying a driving force to the stirring mechanism unit, during the stirring and cooling of the organic gas. Raw An organic matter recovery apparatus, wherein one of the solidified product and the liquefied product is collected in the organic material recovery section.