KR20010044153A - Direction of the wind separated by rotation type rotor for v.o.c treatment equipment - Google Patents

Abstract

PURPOSE: Provided is a rotational rotor for distributing the direction of wind in an organic solvent treater which just rotates a rotary wing in the center to treat large volume of organic solvent so that it reduces the use of energy and power. CONSTITUTION: The rotational rotor for distributing the direction of wind in the organic solvent treater comprises the parts of: an adsorption equipment which adsorbs organic solvent, extrudes purified air with organic solvent adsorbed and desorbs the adsorbed organic solvent; a rotor(100) which consists of a main axis pipe including a first suction or exhaust hole to flow noxious gases in or out, a rotary wing and a second exhaust hole to exhaust the noxious gases flown from the first suction hole; a rotor cover(200) which consists of a separation plate(230) to prevent the noxious gases and clean air from being permeated between a first and a second external hall and a division area to prevent suction or exhaust fluid from being mixed in the center of the separation plate; and a driving tool to rotate the rotor at the assigned low speed.

Description

DIRECTION OF THE WIND SEPARATED BY ROTATION TYPE ROTOR FOR V.O.C TREATMENT EQUIPMENT}

The present invention inhales harmful gases containing organic solvents in a plant generating volatile organic compounds (VOC), adsorbs them into a filtration layer equipped with a fibrous activated carbon filter or a catalyst layer provided with a heat storage layer to purify and clean air. In more detail, the filtering device or the heat storage layer is provided between radially mounted separation plates, and between the upper, lower, and rotary wings of the rotor provided in the center. Noxious gas flows into the first and second suction and discharge ports formed and is adsorbed and purified in the filtration layer. The rotor is rotated and absorbed and desorbed so that the processing power of the organic solvent can be improved by increasing the processing efficiency of the organic solvent. It relates to a rotatable rotor to distribute fragrance.

The present invention is a domestic priority claim application for patent application No. 2000-068444 filed by the applicant of November 17, 2000.

In addition, the present invention by improving the rotor of the "combustion equipment for distributing the wind direction by the rotary rotor" of Utility Model Registration No. 0199716 filed and registered by the present applicant by changing the flow direction of harmful gas and clean air In addition, the present invention relates to a versatile hazardous gas treatment facility that can be used as a heat exchanger when maximizing treatment efficiency and providing a honeycomb heat storage material instead of a filter of a filter layer provided therein.

In general, various devices have been disclosed for adsorbing volatile organic compounds.

1 is a patent application filed and filed by the applicant of the Utility Model Registration No. 0194146-00-00 of the "adsorption device to increase the adsorption of volatile organic compounds", in particular, to improve the driving method of the rotary rotor .

As shown, the cartridge C is divided into a total of 19 compartments, and each filter cell FC stays for 20 seconds, and is repeatedly cycled through adsorption, desorption, and cooling. Continually repeats the process as described above continuously.

As the first to eighth adsorption process, the eighth filter cell (FC) adsorbs an organic solvent, that is, thinner, toluene, ethylbenzene, etc. for 30 seconds. In the adsorption process, the organic solvent is activated carbon. After adsorption and filtering by the filter cell (FC), the fresh air is discharged through the discharge fan (OF).

In addition, after staying 30 seconds in the division zone shown in the next step 9, and moves to the desorption process of 10 to 15 times.

At this time, as described above, the desorbed organic solvent is burned in the combustion facility (FU), and only fresh air is oxidized and discharged into the atmosphere.

The air of 300 ~ 350 ℃ heated in the combustion equipment (FU) is heated to 60 ~ 70 ℃ about the clean air introduced from the outside to move to the above-described desorption process 10 ~ 15, 100 is made of desorption of the right organic solvent In order to heat to a temperature of more than ℃ ℃ goes through a heater (HT) to a temperature that is easy to detach and move to the desorption process (10 ~ 15).

Likewise, the filter cell (FC), which has been cleaned for 10 to 15 times in the same manner and in the same time, stays 30 seconds in the 16th section, and then adsorbs the organic solvent below 40 ° C in the 17th and 18th cooling processes. After cooling to the most ideal temperature below, after 30 seconds in 19 divisions, the same process as described above in the adsorption process from 1 to 8 is repeatedly rotated and filtered.

But. Since the apparatus as described above rotates the entire rotor provided with the filter, a large power is required, and thus the power ratio is excessive compared to the processing capacity.

In addition, the complicated structure of the cartridge provided with the filter is difficult to manufacture, and it is difficult to match the precision of the rotation even after the production is completed, which requires excessive post management cost and man hour after installation. there was.

In addition, a conventional heat exchanger is a tubular or plate heat exchanger, and the heat recovery efficiency is 40 to 50% due to indirect heat exchange. Thus, the hot air passing through the heat exchanger moves to an adsorption facility for desorption. By heating up to hot air once again by such a heater, this also had a problem which leads to waste of excessive energy.

The present invention has been made to solve the problems described above, the object of the present invention is to fix the portion in which the heat storage material of the filter or the heat exchanger is mounted, so that only the rotary wing provided in the center to rotate large capacity It is to provide a device capable of processing organic solvents.

In addition, the other object of the present invention, as described above, can be used as the adsorption equipment when the rotor is rotated so that only the filter, and the heat storage material can be used as a heat exchanger according to the user's choice It is an object of the present invention to provide a multipurpose device in which the purpose of the device is different.

In addition, another object of the present invention is a direct heat exchange method using a heat accumulator of a conventional honeycomb type ceramic when used as a heat exchanger, maintaining a temperature sufficient to desorb an organic solvent even if a separate heater is not provided. To improve efficiency, but to reduce energy consumption.

1 is a reference perspective view showing a schematic diagram of a purification facility equipped with a rotary rotor that rotates simultaneously with a conventional filter.

Figure 2 is an exploded perspective view showing in detail the configuration of the rotor and the rotor cover of the present invention,

3 is a perspective view illustrating the flow of harmful gas and clean air by combining the rotor and the rotor cover of the present invention;

4A and 4B are cross-sectional views taken along the lines “A”-“A” and “B”-”B” of FIG. 3, illustrating the flow of clean air flowing between the rotary gas and the noxious gas flowing into the main shaft pipe. It is a sectional view shown to

5A and 5B are cross-sectional views and perspective views of a line “C”-“C” in FIG. 4, which are illustrated to explain the function of a pipe provided in the main shaft pipe dividing unit.

Figure 6 is an embodiment of the present invention, is a cross-sectional view showing in detail for the adsorption equipment equipped with a rotor of the present invention,

7 is a cross-sectional view showing another embodiment for explaining a heat exchanger equipped with a rotor of the present invention;

8 is a reference diagram illustrating a concentrator and a heat exchanger having a rotor of the present invention and forming one line.

* Explanation of symbols for the main parts of the drawings

100; rotor 101, 102; first and second bearing

101a; first rotating shaft 102a; second rotating shaft

103; first inlet 103a; second inlet

104; first outlet 104a; second outlet

110; spindle tube 120; rotary wing

121; partition 121a; sealing plate

122; blocking membrane 123; adjusting bolt

130; pipe 200; rotor cover

210; first outer hole 220; second outer hole

230; Separator SP; Spring

BG; Hazardous Gases FO1, FO2; Clean Air

HA; Heated air HA1; Low temperature air

UP, DP; upper and lower FA; clean area

According to the present invention, harmful gases generated from volatile organic compounds (VOCs) are introduced into the first duct to adsorb organic solvents into the filtration layer provided therein, and the purified air adsorbed by the organic solvents into the air through the second ducts. And an adsorption system 10 for desorbing the adsorbed organic solvent to the clean air introduced through the third duct and discharging it through the fourth duct.

The adsorption equipment is mounted inside the first and second rotary shafts inserted into the first and second bearings provided at the upper and lower ends, and includes a first suction port and a first discharge port formed to suck and discharge noxious gas on the outer periphery of the upper and lower ends. Hazardous gases formed on one side of the main shaft tube, a plurality of rotary wings are mounted on the upper and lower outer peripheries of the main shaft tube at predetermined equal intervals, and one side of the main shaft tube on which the rotary wings are mounted. The second outlet to discharge the exhaust gas, and the harmful gas discharged from the second outlet through the filtration layer to purify, and then sucked into the second inlet formed on one side of the lower side of the main shaft tube of the main shaft tube A rotor in which a first discharge port is formed to discharge through the inside;

It is provided on the outer lower end of the rotary wing is adsorbed to the filtration layer by the first outer hole and a plurality of first outer holes formed at a predetermined equal interval so that the clean air is introduced, the harmful gas is discharged, and the clean air discharged to the first outer hole The organic solvent is detached and discharged through the second outer hole formed at the upper end, and the separator is mounted between the first and second outer holes to prevent mixing of harmful gas and clean air, and is absorbed in the center of the separator. A rotor cover formed with a partition to prevent mixing of the exhaust fluid;

Drive means for rotating the rotor at a predetermined low speed.

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

Figure 2 is an exploded perspective view showing in detail the configuration of the rotor and the rotor cover of the present invention, Figure 3 is a perspective view illustrating the flow of harmful gas and clean air is coupled to the rotor and the rotor cover of the present invention; 4A and 4B are cross-sectional views taken along the lines “A”-“A” and “B”-”B” of FIG. 3, showing the flow of clean air flowing between the rotary gas and the noxious gas flowing into the main shaft pipe. 5A and 4B are cross-sectional views and perspective views of a line “C” through “C” of FIG. 4, which illustrate the function of a pipe provided in the main shaft pipe segment. 6 is a cross-sectional view illustrating in detail an adsorption system equipped with a rotor of the present invention as an embodiment of the present invention, and FIG. 7 is another embodiment for explaining a heat exchanger equipped with the rotor of the present invention. An example is a sectional view, and FIG. 8 It is a reference figure which shows the enrichment apparatus and heat exchanger which were provided with the rotor of this invention, and formed one line.

Before describing the present invention in detail, the volatile organic compound V.O.C (Volatile Organic Compound) will be briefly described.

The VOC is a hydrocarbon compound having a vapor pressure of 0.02 psi or higher or a boiling point of less than 100 ° C. among organic compounds. It is defined.

V.O.C is a source of harmful air and odors. It is not only harmful to the human body such as inducing carcinogens in the respiratory tract. It also causes environmental pollution as a cause of smog formation and odor generation through photochemical reactions.

Therefore, the method of removing VOC includes combustion oxidation technology, adsorption technology, biological treatment technology, etc., but in the present invention, an adsorption facility having a filtration layer made of an adsorbent and a heat exchanger having a heat storage layer (HS) are provided. Through the rotor 100 applied to the group (HC) will be described a method of recovering a stable treatment of volatile organic compounds (VOC) and high efficiency thermal energy.

2 and 3, the rotor 100 of the present invention is provided with first and second rotary shafts 101a and 102a on the upper and lower ends of the tubular spindle tube 110. Combination with the first and second bearings (bearing) 101 and 102 provided on the upper and lower ends of each treatment facility to be described later to facilitate rotation.

The first copper plate 111 is installed in each of the first and second rotary shafts 101a and 102a to close and seal both ends of the spindle tube 110, and the main shaft is inward of the first copper plate 111. The tube 110 is provided.

The first suction port 103 is formed by the upper outer circumference of the main shaft tube 110 to facilitate the introduction of harmful gas (BG) containing the organic solvent from the surroundings.

On the other hand, a plurality of rotary wings 120 are radially mounted on the lower outer periphery of the first suction port 103, and divided portions are formed on both sides of the central portion divided in half in the cross section of the rotary wing 120. 121 is formed, but one side of the divided part 121 includes a sealing plate 121a having a rectangular opening, and the other side of the dividing part 121 is provided with a completely sealed sealing plate 121a. The structure of the installment 121 will be described in detail with reference to FIG. 4).

A first outlet 104 is formed between the rotary wings 120 mounted on one side of the dividing unit 121, and the first outlet 104 and the second suction port 103a to be described later are It is formed between the rotary wing 120 of one side of the above-described divided portion 121.

At this time, the harmful gas (BG) introduced through the first suction port 103 is introduced into the main shaft pipe 110, discharged through the first discharge port 104 and provided radially filter layer (F). ) Is the adsorption of organic solvent.

In addition, as described above, the purified air BG1 in which the organic solvent is adsorbed is sucked into the second suction port 103a formed between the rotary wings 120 at one side of the splitter 121 provided at the lower side thereof, It exits to the second outlet 104a formed at the lower side through 110 and is discharged to the atmosphere through an exhaust fan (not shown).

The rotary wing 120 provided in the upper portion and the rotary wing 120 provided in the lower portion are provided symmetrically with each other, and the clean air FO1 is provided at the lower portion in the reverse order of the above-described harmful gas (BG) flow. The split part 121 flows into the rotary wing 120 on the other side and flows upward, and the inside of the main shaft pipe 110 having the upper and lower rotary wings 120 is blocked. That is, the noxious gas BG flows through the first discharge port 104 and the second suction port 103a formed on the upper and lower sides of the main shaft pipe 110 on one side of the splitter 121, and the clean air FO1 is formed as described above. It is discharged to the rotary wing 120 provided on the upper side through the rotary wing 120 provided on the other side with respect to the splitter 121.

In addition, the first discharge port 104 and the second suction port 103a formed on one side of the split part 121 through which the noxious gas BG flows are formed, and the blocking film 122 is installed at the lower and lower ends thereof. BG) and the clean air of the clean zone FA of FIG. 3 are essentially blocked.

In addition, the rotor cover 200 provided on the outside of the rotor 100 described above is formed with first and second outer holes 210 and 220 at upper and lower ends of the tubular outer circumference.

The outer partition 201 is formed at the center of the cross section of the rotor cover 200 in which the first and second outer holes 210 and 220 are formed so that the division part 121 of the rotary wing 120 stays. As described above, it is to prevent mixing of harmful gas and clean air.

When the rotor cover 200 is coupled to the rotor 100 described above, the inner cover of the upper and lower blocking layers 122 and the upper and lower ends of the rotor cover 200 come into contact with each other by joining into the blocking film 122. Only the rotor 100 provided with the blocking film 122 rotates and the organic solvent is repeatedly adsorbed and desorbed by the clean air FO1 as described above.

On the other hand, as shown in Figure 3 and 4, the outer periphery of the rotor cover 200, the separating plate 230 is mounted radially at the same angle as the rotary wing 120, the separating plate 230 Is to provide multiple filter cells (FCs) of the "adsorption device which improved the adsorption property of volatile organic compounds" of Utility Model Registration No. 0194146-00-00 filed by the present applicant. .

The reason for having multiple adsorbents, that is, filter cells FC as described above, is to maximize the filtration efficiency by expanding the filtration area by that amount.

In the illustrated filter cell FC, the fibrous activated carbon provided therein is installed in a zigzag to maximize the filtration area as described above.

As shown in the drawings, the flow of harmful gas BG and clean air FO1 is illustrated in more detail. 4A and 4B show the first intake port 103 in cross section, and the harmful gas BG containing the organic solvent is formed through the intake port 103 formed on the outer circumference. A plurality of first outer portions which are introduced into the inner side of the plurality of first outlets 104 and the outer periphery of the rotor cover 200 formed between the rotary wings 120 provided on one side of the division part 121 described above. It is discharged to the hole 210 and flows downward through the filtration layer (F) to be described later, the organic solvent is adsorbed.

In addition, shown in b) shows the flow of the purification air BG1 in which the organic solvent is adsorbed to one side of the partition 121 as described above, and the rotor which is the opposite flow of the above-described harmful gas BG. A second flow is introduced through the second outer hole 220 formed at the bottom of the cover 200, flows into the inside of the main shaft pipe 110 through the second suction port 103a formed at the bottom of the rotor 100, the second formed at the bottom It is discharged to the discharge port 104a is discharged to the atmosphere by the exhaust fan (not shown) through the discharge duct (not shown).

In addition, the organic air adsorbed to the filtration layer (F) to be described later flows upward through the rotary wing 120 provided on the lower side of the rotor 100 on the other side of the splitter 121. Solvent desorption, the upper and lower plate (UP) (DP) is provided with a normal metal plate on the bottom, the blocking film 122 is provided with a clean zone (FA) to prevent mixing with the above-described harmful gas (BG). And, the clean air (FO1) flowing through the third duct (D3) is introduced through the rotary wing 120 provided on the lower side at a temperature of 100 ℃ or more to facilitate the desorption of the organic solvent of the rotor cover 200 It is discharged to the second outer hole 220 formed at the bottom.

In addition, the clean air FO1 passes through the filtration layer F on which the organic solvent is adsorbed as described above, and desorbs the organic solvent and flows into the first outer hole 210 formed on the upper side of the rotor cover 200. It will be discharged through the rotary wing 120 provided on the upper side.

At this time, the organic solvent desorbed into the clean zone FA having the upper and lower plates UP and DP as described above is discharged, and the organic solvent remaining in the clean zone FA is the fourth duct. It is discharged through D4 (not shown).

In addition, although only one filter cell FC has been shown and described in the drawing, in the actual field, all are provided between the separators 230 so as to be adsorbed and pressed to one side based on the splitter 121. Desorption is repeated on the side, and the above-mentioned adsorption and desorption are repeated by the rotation of the rotor 100 continuously rotating.

According to (a) and (b) of FIG. 5, clean air FO2 flows into the clean air inlet 101b (hereinafter, referred to as an “inlet”) formed in the first rotating shaft 101a provided below. The pipe 130 is provided on the upper side, and is discharged to one side of the dividing unit 121 divided in half on the cross section of the rotor 100 as described above, and the other side of the pipe 130 has a closed front structure. Is not provided.

In addition, the reason for discharging the clean air FO2 through the pipe 130 is when the partition 121 and the separation plate 230 crosses by the rotation of the rotor 100 to the separation plate 230. By pushing the residual noxious gas to the upper part, the noxious gas (BG) is prevented from remaining so that when the clean air (FO1) is introduced in the next process, the treatment efficiency is improved.

That is, the filter layer (F) at the discharge pressure of the clean air (FO2) through the pipe 130 described above to the residual harmful gas (BG) inside the separator plate 230 through which the harmful gas has passed through the harmful gas (BG). By sending it to the top of the), the separation plate 230 is to prevent harmful gas (BG) is left to prevent the mixing with the newly introduced clean air (FO1) by the rotation of the rotor 100 is essentially. .

In addition, the divided part through which the clean air is discharged by the pipe 130 is provided with a sealing plate (121a) to maintain the compressed state by the spring (SP) to the outer partition 201 of the rotor cover 200 It is to be in close contact with the inside of the, and not to contact is the sealing plate 121a adjusted in position by the adjustment bolt 123 shown is fixed without movement.

6 to 8, the rotor 100 of the present invention is provided, and the adsorption facility 10 and the heat exchanger HC including the filtration layer F are provided at the center of the rotor 100. It is.

As shown in FIG. 6, the noxious gas BG introduced through the first duct D1 flows downward as described above, and the organic solvent is adsorbed through the filtration layer F. Completed clean air is discharged into the atmosphere through the second duct D2 and the exhaust fan (not shown) through the second outlet 104a.

In addition, the clean air FO1 heated to a temperature of 100 ° C. or more through the heat exchanger HC, which will be described later with reference to FIG. 7, is introduced through the third duct D3 and the rotary wing 120 at the other side of the division part 121 described above. ) To desorb the organic solvent adsorbed on the filtration layer (F) provided between the separation plate 230 is discharged through the fourth duct (D4).

In addition, the discharged organic solvent is sent to a combustion facility (FU), not shown, to be burned by a burner (not shown), and to send heated air having a temperature of 450 ° C. or higher by the burner to the heat exchanger HC. 1 to 4 ducts (D1 to D4) are described by attaching the same names and the same symbols to the adsorption facility 10 and the heat exchanger HC.)

As shown in FIG. 7, a honeycomb-type ceramic (hereinafter, referred to as a "heat storage layer (HS)") is provided between the separators 230 so that one side of the separator is a combustion facility ( The heating air (450 ℃ or more) (HA) after burning the organic solvent from the (not shown) flows into the first duct (D1) to increase the temperature of one side divided by the heat storage layer (HS) in half and the heat storage layer The low temperature air HA1 deprived of heat to the HS is discharged into the atmosphere through the second duct D2.

In addition, the clean air FO1 introduced through the third duct D3 is upper through the rotary wing 120 provided in the clean area FA provided with the upper and lower plates UP, as described above. It flows into, and is discharged to the lower portion of the heat storage layer (HS) shown through the second outer hole 220 formed at the bottom of the rotor cover (200).

In addition, the clean air FO1 in the atmosphere is heated to a temperature of about 100 ° C. or more while passing through the heat storage layer HS heated by the heating air HA of 450 ° C. or higher in the combustion facility FU, and thus the fourth duct ( D4) is sent to the above-mentioned adsorption facility 10 to desorb the organic solvent adsorbed on the filtration layer (F).

At this time, as the temperature rises above 100 ° C. moves to the adsorption facility 10, desorption of the organic solvent adsorbed onto the filtration layer F of the adsorption facility 10 is performed without using a separate heater HT. It is to facilitate the process, and to repeat the above process.

As described above, the heat exchanger HC equipped with the rotor 100 of the present invention serves to heat up the clean air FO1 introduced from the outside, so that the thermal efficiency of the heat exchanger HC is higher than that of the conventional tubular or plate heat exchanger. 90 to 95% of the thermal efficiency can be obtained.

In addition, the rotor 100 of the present invention rotates at a low speed of at least 4 revolutions per minute in the drive means 300 provided on one side of the lower side, and repeats the adsorption and desorption of the organic solvent as described above, and the heat exchanger ( HC) is heat-generated heat storage layer (HS) by the heating air (HA) of 450 ℃ or more, and generates heat by the low-temperature clean air (FO1) in the air as described above, the radial filtration The layer F and the heat storage layer HS can be used almost semi-permanently by repeating the above-described operation evenly by the rotor 100 of the present invention which rotates at a low speed, and thus has a cost reduction effect.

FIG. 8 is a reference diagram showing a processing facility in which one line is formed as described above.

The organic solvent adsorbed to the filtration layer F of the adsorption equipment is desorbed by the clean air FO1 introduced by the rotating rotor 100, and the desorbed organic solvent is sent to the combustion equipment FU for combustion. The heated air is discharged into the atmosphere by heating air deprived of heat to the heat storage layer (H) through the heat exchanger (HC) provided with the rotary rotor (100) of the present invention, and the heated heat storage layer (H) flows from one side. The mixture is mixed with clean air and the temperature is raised to a temperature of 100 ° C. or higher, and the heated air is sent back to the adsorption facility equipped with the rotary rotor 100 to repeat the process of desorbing the organic solvent.

The present invention is not limited to the above-described specific preferred embodiments and can be easily modified by anyone of ordinary skill in the art without departing from the gist of the invention claimed in the claims. Such changes are intended to fall within the scope of the claims.

According to the present invention, it is possible to fix the site where the heat storage material of the filter or the heat exchanger is mounted, and to rotate only the rotary wing provided in the center, thereby supplying a device capable of processing a large amount of organic solvent with a small power, thereby providing a sense of confidence to users Has given effect.

In addition, as described above, only the rotary wing can be rotated so that a filter can be used as an adsorption facility, and when a heat storage material is provided, a heat exchanger can be used as a heat exchanger. The effect of providing the device is effective.

In addition, the heat exchanger having a heat recovery efficiency of 90 to 95% eliminates the need for a separate heater, thereby reducing unnecessary energy and power waste.

In addition, it is possible to semi-permanently use the life of the filtration layer (F) and the heat storage layer (HS) by repeating the adsorption and desorption, heat storage and heat generation by the rotation has the effect of reducing the cost. .

Claims (8)

The harmful gas generated from volatile organic compounds (VOC) is introduced into the first duct to adsorb the organic solvent into the filtration layer provided therein, and the purified air to which the organic solvent is adsorbed is discharged into the atmosphere through the second duct. In the adsorption facility 10 for desorbing the adsorbed organic solvent to the clean air introduced through the third duct to discharge through the fourth duct, The adsorption equipment is mounted inside the first and second rotary shafts inserted into the first and second bearings provided at the upper and lower ends, and includes a first suction port and a first discharge port formed to suck and discharge noxious gas on the outer periphery of the upper and lower ends. Hazardous gases formed on one side of the main shaft tube, a plurality of rotary wings are mounted on the upper and lower outer peripheries of the main shaft tube at predetermined equal intervals, and one side of the main shaft tube on which the rotary wings are mounted. The second outlet to discharge the exhaust gas, and the harmful gas discharged from the second outlet through the filtration layer to purify, and then sucked into the second inlet formed on one side of the lower side of the main shaft tube of the main shaft tube A rotor in which a first discharge port is formed to discharge through the inside; It is provided on the outer lower end of the rotary wing is adsorbed to the filtration layer by the first outer hole and a plurality of first outer holes formed at a predetermined equal interval so that the clean air is introduced, the harmful gas is discharged, and the clean air discharged to the first outer hole The organic solvent is detached and discharged through the second outer hole formed at the upper end, and the separator is mounted between the first and second outer holes to prevent mixing of harmful gas and clean air, and is absorbed in the center of the separator. A rotor cover formed with a partition to prevent mixing of the exhaust fluid; And a driving means configured to rotate the rotor at a predetermined low speed. The rotary rotor of claim 1, wherein the filter agent provided in the filter layer is a filter cell in which multiple fibrous activated carbons are mounted to maximize the filtration area. According to claim 1, wherein the rotor is mixed between the harmful gas flowing through the second discharge port and the second suction port between the rotary wing of one side, based on the split portion, and the flow of clean air flowing through the other rotary wing at the same time Rotary rotor for distributing the wind direction of the organic solvent processing equipment, characterized in that not. The rotary rotor of claim 1, wherein the divided parts are formed at both sides of the central portion of the rotary wing to prevent mixing of harmful gas and clean air. According to claim 4, One side of the partition is closed, the other side is a closed plate is open, the inside is provided with a pipe to discharge the clean air introduced through the clean air inlet port to the top of the harmful gas remaining between the separation plate Rotary rotor for distributing the wind direction of the organic solvent processing equipment, characterized in that to prevent mixing with fresh air introduced by sending to. The method of claim 5, wherein the sealing plate is in close contact with the inside of the rotor cover in accordance with the elastic force of the compression spring and the tightening degree of the adjustment bolt is adjusted to prevent mixing of the harmful gas and clean air of the organic solvent treatment facility. Rotary rotor for distributing wind direction. The rotary rotor of claim 1, wherein the adsorption equipment is used as a heat exchanger if the honeycomb-type ceramic, which is a normal heat storage material, is used instead of the filtration layer. According to claim 1, wherein the separation plate is mounted radially at the same angle as the rotary wing around the rotor cover to distribute the wind direction of the organic solvent processing equipment, characterized in that to separate the flow of harmful gas and clean air. Typical rotor.