WO2018173714A1 - Exhaust separation device - Google Patents

Exhaust separation device Download PDF

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Publication number
WO2018173714A1
WO2018173714A1 PCT/JP2018/008267 JP2018008267W WO2018173714A1 WO 2018173714 A1 WO2018173714 A1 WO 2018173714A1 JP 2018008267 W JP2018008267 W JP 2018008267W WO 2018173714 A1 WO2018173714 A1 WO 2018173714A1
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Prior art keywords
sewage
exhaust gas
storage tank
water
useful
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PCT/JP2018/008267
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French (fr)
Japanese (ja)
Inventor
京史 寺本
仁 里見
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京史 寺本
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Priority claimed from JP2017151277A external-priority patent/JP2018158329A/en
Application filed by 京史 寺本 filed Critical 京史 寺本
Publication of WO2018173714A1 publication Critical patent/WO2018173714A1/en

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  • the present invention relates to an exhaust separation device.
  • the following devices have been proposed as devices for reducing the volume of a processing object containing an organic substance or obtaining a useful substance from a processing object containing an organic substance.
  • a superheated steam carbonization apparatus (superheated steam carbonization furnace) that heats and carbonizes a processing object using superheated steam to obtain a carbide as a useful product (see Patent Document 1).
  • a smoldering-type volume reduction processing device that obtains ash (ceramics) as a useful product by smokeless combustion (sintered), in other words, thermal decomposition of the processing object (see Patent Document 2).
  • exhaust gas is generated by heating or thermally decomposing an object to be treated containing organic matter.
  • Such exhaust gases contain useful oils and ash, which can be reused as paints, fuels and resin materials, and ash can be reused as building aggregates and admixtures. It is desired to efficiently separate useful substances.
  • the present invention has been made in view of the above circumstances, and provides an exhaust gas separation apparatus that is advantageous in efficiently separating and recovering useful materials from exhaust gas generated during processing of an object to be processed including organic matter. With the goal.
  • the present invention is an exhaust separation device that separates the useful material from the exhaust gas containing the useful material, the duct forming a flow path through which the exhaust gas flows, and an interval in the duct in which the exhaust gas flows.
  • a plurality of grease filters arranged to adsorb the useful materials, a cleaning unit for cleaning the useful materials adsorbed on the grease filters by injecting cleaning water to the respective grease filters, and jetting the cleaning water
  • a storage tank for storing sewage containing the useful material flowing down from each grease filter, and a recovery unit for discharging the sewage remaining after recovering the useful material from the sewage stored in the storage tank, Filtration water is obtained by filtering the sewage by adsorbing the useful material by the porous material from the sewage that contains the porous material that adsorbs the useful material and is discharged from the recovery unit.
  • a filtration tank to be generated characterized in that it comprises said filtered water the supply unit for supplying the filter tank to the washing unit as the cleaning water.
  • the present invention when exhaust gas passes through a plurality of grease filters, useful substances of the exhaust gas are efficiently adsorbed by the plurality of grease filters, so it is of course possible to perform exhaust that has little odor and does not affect the environment.
  • This is advantageous in efficiently separating and recovering useful substances from exhaust gas generated during the treatment of the object to be treated including organic substances.
  • each grease filter is washed with washing water, the adsorption performance of useful materials by the grease filter is well maintained, which is more advantageous in efficiently separating and recovering useful materials from exhaust gas.
  • useful substances are recovered from the sewage obtained by washing the grease filter, it is advantageous in efficiently separating and recovering useful substances from the exhaust gas.
  • oil can be reused for fuel, paint and resin material, and ash can be reused as building aggregate and admixture.
  • the useful material that has been emulsified in the sewage is adsorbed and removed by the porous material in the filtration tank, so that filtered water that does not contain useful material can be obtained. Since it can be reused as cleaning water, it is advantageous in saving cleaning water.
  • the exhaust separation device 12 separates useful oils and ash from exhaust gas discharged from the treatment device 10 that treats a processing object including organic matter, and the useful matter is separated.
  • the exhaust gas purified by the above is discharged into the atmosphere as exhaust gas.
  • the processing target containing organic matter is not limited to waste containing organic matter typified by waste plastic and garbage, but various kinds of trees such as thinned wood, bark of trees, algae, etc. It shall contain organic matter.
  • the processing apparatus 10 to which the exhaust gas separation apparatus 12 of the present invention is applied may be any apparatus that generates exhaust gas by processing a processing target including organic matter.
  • the processing target including organic matter using superheated steam is used.
  • Conventionally known devices such as a superheated steam carbonization device that heats and carbonizes, a fire burning type volume reduction processing device that thermally decomposes a processing object containing organic matter, or an incineration device that incinerates a processing object containing organic matter
  • the present invention can be applied to various processing apparatuses.
  • the exhaust separation device 12 includes an exhaust gas treatment unit 14, a first recovery unit 16, a second recovery unit 18, a filtration tank 20, a supply unit 22, a cleaning unit 24, and the like.
  • the exhaust gas processing unit 14 includes an exhaust fan 26, a duct 28, a plurality of grease filters 30, a shower nozzle 32, a shower pump 34, an upper storage tank 36, and a lower storage tank 38.
  • the exhaust fan 26 sucks the exhaust gas discharged from the processing apparatus 10 through the duct 28 and sends it to a chimney (not shown).
  • the duct 28 forms a flow path F through which exhaust gas flows. As shown in FIGS.
  • the duct 28 includes a rectangular plate-like upper wall 2802 extending along the horizontal direction, and an upper wall 2802.
  • a pair of side walls 2804 extending downward from both sides in the longitudinal direction of the upper wall 2802, an upstream end wall 2806 extending downward from an end located on the upstream side of the flow of exhaust gas among the longitudinal ends of the upper wall 2802,
  • a downstream end wall 2808 extending downward from an end located on the downstream side of the exhaust gas flow of both ends in the longitudinal direction of the upper wall 2802, the upper wall 2802, a pair of side walls 2804, an upstream end wall 2806,
  • a flow path F is formed by the downstream end wall 2808.
  • a through hole 2806A is formed in the upstream end wall 2806, and this through hole 2806A is connected to the processing apparatus 10 through a pipe line 2812.
  • a damper (not shown) is provided.
  • a through hole 2808A is formed in the downstream end wall 2808, and this through hole 2808A is connected to the exhaust fan 26 via a pipe line 2814.
  • the pipe line 2814 is provided with a damper (not shown) for adjusting the air volume. ing.
  • the exhaust gas discharged from the processing apparatus 10 flows through the flow path F of the duct 28 from the upstream end wall 2806 side to the downstream end wall 2808 side via the pipe line 2812. It is led from the pipe line 2814 to the chimney through the exhaust fan 26 and discharged into the atmosphere.
  • the grease filter 30 includes a filter body 3002, a pair of nets 3004, and a frame portion 3006.
  • the filter body 3002 adsorbs useful substances of exhaust gas, is composed of metal fibers, and has a rectangular plate shape.
  • the metal fiber has, for example, a cotton shape, a fabric shape, or a three-dimensional network.
  • aluminum is used as such a metal fiber, and durability is improved.
  • metal fibers using various conventionally known metal materials can be used.
  • the pair of nets 3004 covers both surfaces of the filter body 3002 in the thickness direction, and is configured by a rectangular metal net.
  • the frame portion 3006 holds the filter body 3002 and the pair of metal nets 3004, and is a metal plate that extends in a frame shape along the outer edges of the filter body 3002 and the pair of metal nets 3004. It is configured.
  • the plurality of grease filters 30 are arranged in parallel with each other at equal intervals along the direction in which the exhaust gas flows, and are attached to the inner surface of the duct 28 via a bracket (not shown).
  • nine grease filters 30 are provided.
  • the upper edge of each grease filter 30 is in contact with the inner surface of the upper wall 2802 of the duct 28 without a gap, and a pair of side edges connected to both ends of the upper edge of each grease filter 30 and extending vertically are provided on the duct 28.
  • a pair of side walls 2804 are in contact with the inner surfaces of the pair of side walls 2804 without any gap.
  • each grease filter 30 is cleaned with the grease filter 30 stored in the upper storage tank 36 through the opening 2810 of the duct 28. It is in a state immersed in the sewage W2. Therefore, the flow path F in the duct 28 is formed in a space surrounded by the inner surface of the upper wall 2802 of the duct 28, the inner surfaces of the pair of side walls 2804, and the water surface of the dirty water W2. In other words, the flow path F is comprised by the inner surface except the bottom part of the duct 28, and the water surface of the sewage W2.
  • the shower nozzle 32 is disposed in the space between the adjacent grease filters 30 inside the duct 28.
  • the useful water adsorbed by the grease filter 30 is washed by spraying the washing water W1 toward the surface.
  • the washing water W1 sprayed from the shower nozzle 32 becomes a mist by vigorously colliding with the grease filter 30 and the wall surface (inner surface) of the duct 28, and the flow path F is filled with the mist.
  • Such mist adsorbs useful substances in the exhaust gas and falls downward to improve the purification efficiency of the exhaust gas.
  • mist in order to promote generation
  • a charging unit that positively or negatively charges the generated mist may be provided so that useful substances can be more efficiently adsorbed to the mist.
  • mist has the property to adsorb
  • the shower pump 34 supplies the cleaning water W1 stored in the filtration tank 20 to each shower nozzle 32 via a pipe 35 (see FIGS. 2 and 4A).
  • each shower nozzle 32 and shower pump 34 constitute a cleaning unit 24 that cleans useful materials adsorbed on the grease filter 30 by injecting cleaning water W1 to each grease filter 30, and a duct. It functions as a mist generating part that generates mist in the duct 28 by injecting water into the 28.
  • the upper storage tank 36 includes a rectangular plate-like bottom wall 3602 having a larger outline than the duct 28 in a plan view and extending in the horizontal direction, and a bottom.
  • the wall 3602 includes a pair of side walls 3604 erected from both sides in the longitudinal direction and a pair of end walls 3606 erected from both ends of the bottom wall 3602 in the longitudinal direction.
  • the upper portion of the upper storage tank 36 has an opening 3608. .
  • the upper storage tank 36 accommodates the lower part of the duct 28 through the opening 3608 in a state in which the longitudinal direction thereof coincides with the longitudinal direction of the duct 28, and the lower edge of the duct 28 (a pair of side walls 2804, an upstream end wall).
  • the lower edge of the downstream end wall 2808) is located below the upper edge of the upper storage tank 36 (the upper edges of the pair of side walls 3604 and the pair of end walls 3606).
  • a partition wall 3610 extending perpendicularly to the longitudinal direction of the bottom wall 3602 and extending between the pair of side walls 3604 is located at a position nearer to the longitudinal direction of the bottom wall 3602 and outside the downstream end wall 2808 of the duct 28.
  • the upper edge 3610A of the partition wall 3610 is positioned below the upper edge of the upper storage tank 36.
  • a through hole 3612 is formed in the portion of the bottom wall 3602 located between the partition wall 3610 and the end wall 3606 near the partition wall 3610.
  • the cleaning water is sprayed from the shower nozzle 32 to the grease filter 30, so that the sewage containing useful substances flows down from the grease filter 30 and is stored in the upper storage tank 36, and then the sewage W2 stored in the upper storage tank 36.
  • the sewage W2 flows down to the bottom wall 3602, and flows out downward through the through hole 3612.
  • the height of the upper edge 3610A of the partition wall 3610 is set so that the surface of the sewage W2 stored in the upper storage tank 36 is located above the lower edge 30A of the grease filter 30. By doing so, the lower part of the grease filter 30 is immersed in the sewage W2 stored in the upper storage tank 36.
  • the lower storage tank 38 is provided in the lower part of the upper storage tank 36, and stores the sewage W2 flowing down from the lower storage tank 38 through the through hole 3612.
  • the lower storage tank 38 stands from a rectangular plate-like bottom wall 3802 extending along the horizontal direction, a pair of side walls 3804 standing from both longitudinal sides of the bottom wall 3802, and both ends of the bottom wall 3802 in the longitudinal direction.
  • a pair of end walls 3806 is provided, and the upper part of the lower storage tank 38 is an opening 3808 opened upward.
  • the lower storage tank 38 is provided so that most of the bottom wall 3602 including the through hole 3612 of the upper storage tank 36 is located inside the opening 3808 of the lower storage tank 38.
  • the upper storage tank 36 and the lower storage tank 38 comprise the storage tank which stores the waste water W2 containing the useful material which flows down from each grease filter 30 by injecting the wash water W1.
  • the first recovery unit 16 sucks the supernatant of the sewage W2 stored in the lower storage tank 38, recovers useful materials from the sewage W2, and returns the remaining sewage W2 to the lower storage tank 38.
  • the sewage W2 is circulated in the lower storage tank 38. 2 and 3, the first collection unit 16 is not shown.
  • a first recovery unit 16 for example, a commercially available product such as a floating oil recovery device (model number DS1-120) of Terada Pump Manufacturing Co., Ltd. can be used.
  • the first recovery unit 16 includes a compressor 17. The compressor 17 injects air into the sewage W2 stored in the lower storage tank 38.
  • the second recovery unit 18 is useful from sewage W2 located below the surface of the sewage W2 stored in the lower storage tank 38 or near the bottom wall 3802 of the lower storage tank 38.
  • the remaining sewage W2 is discharged.
  • the first feed pump 42 is provided on the bottom wall 3802 of the lower storage tank 38, and is positioned below the water surface of the sewage W ⁇ b> 2 in the lower storage tank 38.
  • the sewage W2 is fed to the second recovery unit 18 via the first feed pump 42 and the pipe 43.
  • the following principle can be used as the second recovery unit 18.
  • a cylindrical filter 1802 having an axial center extending in the horizontal direction is rotated in one direction by a motor 1804, and the sewage W2 is passed from the radially outer side to the radially inner side of the filter 1802 so that the outer surface of the filter 1802 has The useful substance contained in W2 is adhered.
  • a transfer roll 1806 having an axial center parallel to the filter 1802 and having a cylindrical surface that contacts the outer peripheral surface of the filter 1802 is brought into contact with the filter 1802, and the transfer roll 1806 is rotated by the filter 1802 while maintaining the contact state. Following rotation, useful materials on the outer peripheral surface of the filter 1802 are attached to the outer peripheral surface of the transfer roll 1806.
  • the tip of the doctor 1808 is brought into contact with the outer peripheral surface of the transfer roll 1806 and the useful material is collected by scraping the useful material from the outer peripheral surface of the transfer roll 1806 by the doctor 1808.
  • the sewage W2 that has passed through the filter 1802 is discharged from the second recovery unit 18.
  • recovery part 18 commercial items, such as a brand name new type eco filter of Satomi Manufacturing Co., Ltd., can be used, for example.
  • the filter 1802 is formed using a mesh formed of a photocatalytic material (eg, titanium oxide), and an ultraviolet light source 1810 that irradiates ultraviolet light toward the filter 1802 is provided.
  • the chemical substance contained in the sewage W2 is decomposed by the filter 1802 (photocatalyst material) activated by irradiating ultraviolet rays, and thus, for example, harmful chemical substances contained in the sewage W2 are detoxified.
  • the second recovery unit 18 includes a photocatalyst processing unit 19 that decomposes a chemical substance contained in the sewage W2 using a photocatalyst material and ultraviolet light.
  • the photocatalyst processing unit 19 includes the filter 1802 and the ultraviolet light. And a light source 1810.
  • the photocatalyst processing unit 19 only needs to be able to decompose the chemical substance contained in the sewage W2 by using a photocatalyst material, and conventionally known such as contacting the sewage W2 while irradiating the photocatalyst material provided separately from the filter 1802 with ultraviolet light Various configurations can be adopted.
  • the second recovery unit 18 recovers useful materials mixed in the sewage W2 without floating on the surface of the sewage W2, but cannot recover useful materials that are emulsified and dissolved in the sewage W2.
  • the filtration tank 20 contains a porous material (not shown) that adsorbs a useful material and adsorbs the useful material from the sewage W2 discharged from the second recovery unit 18 by the porous material. Then, the sewage W2 is filtered to produce filtered water.
  • the sewage W2 discharged from the second recovery unit 18 is fed to the filtration tank 20 via the second feed pump 44 and a pipe (not shown). The sewage W2 is stored in the filtration tank 20.
  • porous material for example, a commercially available product such as Y-CUBE, which is a microorganism-immobilized PVA (Polyvinyl Alcohol) carrier (polyvinyl alcohol carrier) of Yukigaya Chemical Co., Ltd., can be used.
  • PVA Polyvinyl Alcohol
  • the useful material that has been emulsified and dissolved in the sewage W ⁇ b> 2 is adsorbed by the porous material, so that filtered water from which the useful material has been removed is obtained.
  • the supply unit 22 supplies the filtered water generated in the filtration tank 20 as the cleaning water W1 from the filtration tank 20 to the cleaning unit 24.
  • the supply unit 22 includes a shower pump 34. Yes.
  • cleans a porous material by inject
  • the porous material is cleaned every predetermined time. At this time, the porous material is contaminated by washing the porous material with filtered water. 2 to the collecting unit 18. Therefore, the useful substance adsorbed on the porous material is separated and recovered by the second recovery unit 18.
  • the third feed pump 46 constitutes a feed unit that feeds filtered water contaminated by the cleaning of the porous material by the cleaning unit 24 to the second recovery unit 18.
  • the cleaning water W1 In order to circulate the cleaning water W1, filtered water, and sewage W2 in the exhaust separation device 12, it is necessary to store a predetermined amount of water in the filtration tank 20, the upper storage tank 36, and the lower storage tank 38 in advance. It is. Further, the amount of water contained in the exhaust gas is adsorbed by the cleaning water W1 for cleaning the grease filter 30, so that the total amount of water circulating in the exhaust separation device 12 increases with the passage of time. Good. For example, when the water stored in the filtration tank 20 exceeds a specified amount, the filtered water exceeding the specified amount may be discharged.
  • the first collection unit 16 sucks the supernatant of the sewage W2 stored in the second storage tank 38 to collect useful materials from the sewage W2 and stores the remaining sewage W2 in the second storage.
  • the sewage W2 is circulated in the second storage tank 38 by returning to the tank 38, and the sewage W2 stored in the second storage tank 38 by the second recovery unit 18 is located below the supernatant. The useful material was recovered from W2 and the remaining sewage W2 was discharged.
  • the bottom part of the duct 28 was formed with the sewage W2 by immersing the lower part of the grease filter 30 in the sewage W2 stored in the storage tank, but the bottom wall of the duct 28 may be provided separately. good. In this case, a configuration for discharging the sewage W2 from the bottom wall 3802 of the duct 28 while maintaining the negative pressure in the duct 28 may be provided.
  • the present embodiment there is no need to provide a configuration for maintaining the negative pressure in the duct 28, which is advantageous in simplifying the configuration of the duct 28 and achieving compactness.
  • the porous material is washed by injecting air into the sewage W2 stored in the filtration tank 20, the equipment required for washing the porous material can be minimized, This is advantageous for reducing equipment costs.
  • the useful material can be further separated and recovered by supplying the filtered water contaminated by the cleaning of the porous material to the second recovery unit 18, it is more advantageous in efficiently separating the useful material from the exhaust gas.
  • the oil content among useful substances separated from the exhaust gas will be described.
  • the incinerated organic matter changes to charcoal, and the generated exhaust gas (smoke) contains water and ash.
  • the generated exhaust gas (smoke) contains water, dry distillation gas, and a slight oil component.
  • the treated organic matter changes to ceramic (ash) and the generated exhaust gas (smoke) includes water, dry distillation Gas and oil containing impurities are included. Since the dry distillation gas contains a combustion gas such as carbon monoxide, the combustion gas can be used as a fuel.
  • the ratio of hydrocarbons contained in the oil recovered from the exhaust gas of the smoldering type volume reduction processing apparatus using the exhaust separation device 12 of the present embodiment is the same as that of general crude oil, and the amount of heat corresponding to crude oil. It is possible to collect the oil component having a useful product. Therefore, when a smoldering type volume reduction processing apparatus is used as the processing apparatus 10, it is extremely difficult to efficiently collect oil corresponding to crude oil as a useful product by using the exhaust separation apparatus 12 of the present embodiment. It is advantageous. Furthermore, if waste plastics, thinned wood, bark, etc., which are low in cost and contain a large amount of hydrocarbons, are treated with a fire burning type volume reduction treatment device, the oil equivalent to crude oil is more efficiently treated. It can be recovered and is advantageous in obtaining a cheap and high value-added useful product.

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  • Water Treatment By Sorption (AREA)

Abstract

The present invention makes it possible to efficiently separate and recover useful material from exhaust gas generated through treatment of an article to be treated that includes organic matter. A plurality of grease filters 30 are arranged in a line in parallel with each other in a duct 28 at even intervals along the direction of flow of exhaust gas. Soiled water that includes useful material flows downward from the grease filters 30 by the grease filters 30 being sprayed with cleaning water from the shower nozzles 32 and is retained in an upper retention tank 36. A first collecting unit 16 circulates soiled water W2 within a lower retention tank 38 by sucking the supernatant of the soiled water W2 retained in the lower retention tank 38, recovering useful material from the soiled water W2, and returning the remaining soiled water W2 to the lower retention tank 38. A second recovery unit 18 recovers useful material from the soiled water W2 located below the supernatant out of the soiled water W2 retained in the lower retention tank 38. A filter tank 20 filters the soiled water W2 and generates filtered water by adsorbing useful material from the soiled water W2 discharged from the second recovery unit 18 using a porous material.

Description

排気分離装置Exhaust separator
 本発明は排気分離装置に関する。 The present invention relates to an exhaust separation device.
 有機物を含む処理対象物を減容化し、あるいは、有機物を含む処理対象物から有用物を得る装置として例えば以下のようなものが提案されている。
 過熱水蒸気を用いて処理対象物を加熱して炭化させ、炭化物を有用物として得る過熱水蒸気炭化装置(過熱水蒸気炭化炉)(特許文献1参照)。
 処理対象物を無煙燃焼(燻焼)、言い換えると熱分解することにより灰(セラミックス)を有用物として得る燻焼式減容化処理装置(特許文献2参照)。
For example, the following devices have been proposed as devices for reducing the volume of a processing object containing an organic substance or obtaining a useful substance from a processing object containing an organic substance.
A superheated steam carbonization apparatus (superheated steam carbonization furnace) that heats and carbonizes a processing object using superheated steam to obtain a carbide as a useful product (see Patent Document 1).
A smoldering-type volume reduction processing device that obtains ash (ceramics) as a useful product by smokeless combustion (sintered), in other words, thermal decomposition of the processing object (see Patent Document 2).
特開2001-214177号公報JP 2001-214177 A 特許第4580388号公報Japanese Patent No. 4580388
 上記従来技術では、有機物を含む処理対象物を加熱、あるいは、熱分解させることによって排ガスが発生する。
 このような排ガスには有用物である油分や灰分が含まれており、油分は塗料、燃料、樹脂材料として再利用でき、灰分は建築用の骨材、混和剤として再利用できるため、排ガスから有用物を効率的に分離することが望まれている。
 本発明は、上記事情に鑑みてなされたものであり、有機物を含む処理対象物の処理に伴って発生する排ガスから有用物を効率的に分離回収する上で有利な排気分離装置を提供することを目的とする。
In the above prior art, exhaust gas is generated by heating or thermally decomposing an object to be treated containing organic matter.
Such exhaust gases contain useful oils and ash, which can be reused as paints, fuels and resin materials, and ash can be reused as building aggregates and admixtures. It is desired to efficiently separate useful substances.
The present invention has been made in view of the above circumstances, and provides an exhaust gas separation apparatus that is advantageous in efficiently separating and recovering useful materials from exhaust gas generated during processing of an object to be processed including organic matter. With the goal.
 本発明は、有用物を含む排ガスから前記有用物を分離する排気分離装置であって、前記排ガスが流れる流路を形成するダクトと、前記ダクト内に、前記排ガスの流れる方向に間隔をおいて並べられた、前記有用物を吸着する複数のグリスフィルタと、前記各グリスフィルタに洗浄水を噴射することで前記グリスフィルタに吸着された前記有用物を洗浄する洗浄部と、前記洗浄水を噴射することで前記各グリスフィルタから流下する前記有用物を含む汚水を貯留する貯留槽と、前記貯留槽に貯留された前記汚水から前記有用物を回収し残った前記汚水を排出する回収部と、前記有用物を吸着する多孔質材料が収容され前記回収部から排出される前記汚水から前記多孔質材料によって前記有用物を吸着することで前記汚水のろ過を行ないろ過水を生成するろ過槽と、前記ろ過水を前記洗浄水として前記ろ過槽から前記洗浄部に供給する供給部とを備えることを特徴とする。 The present invention is an exhaust separation device that separates the useful material from the exhaust gas containing the useful material, the duct forming a flow path through which the exhaust gas flows, and an interval in the duct in which the exhaust gas flows. A plurality of grease filters arranged to adsorb the useful materials, a cleaning unit for cleaning the useful materials adsorbed on the grease filters by injecting cleaning water to the respective grease filters, and jetting the cleaning water A storage tank for storing sewage containing the useful material flowing down from each grease filter, and a recovery unit for discharging the sewage remaining after recovering the useful material from the sewage stored in the storage tank, Filtration water is obtained by filtering the sewage by adsorbing the useful material by the porous material from the sewage that contains the porous material that adsorbs the useful material and is discharged from the recovery unit. A filtration tank to be generated, characterized in that it comprises said filtered water the supply unit for supplying the filter tank to the washing unit as the cleaning water.
 本発明によれば、排ガスが複数のグリスフィルタを通過すると排ガスの有用物が複数のグリスフィルタによって効率的に吸着されるため、臭気が少なく環境に影響を与えない排気を行なうことができることは無論のこと、有機物を含む処理対象物の処理に伴って発生する排ガスから有用物を効率的に分離回収する上で有利となる。
 また、各グリスフィルタは洗浄水によって洗浄されるため、グリスフィルタによる有用物の吸着性能が良好に維持されるため、排ガスから有用物を効率的に分離回収する上でより有利となる。
 また、グリスフィルタを洗浄することで得られた汚水から有用物を回収するようにしたので、排ガスから有用物を効率的に分離回収する上で有利となる。
 また、回収部により排ガスから分離された有用物のうち油分は、燃料、塗料、樹脂材料に再利用でき、灰分は建築用の骨材、混和剤として再利用することができる。
 また、汚水に含まれるエマルジョン化した有用物はろ過槽で多孔質材料によって吸着され取り除かれることで有用物を含まないろ過水を得ることができ、このような清浄なろ過水をグリスフィルタを洗浄する洗浄水として再利用できるため、洗浄水の節約を図る上で有利となる。
According to the present invention, when exhaust gas passes through a plurality of grease filters, useful substances of the exhaust gas are efficiently adsorbed by the plurality of grease filters, so it is of course possible to perform exhaust that has little odor and does not affect the environment. This is advantageous in efficiently separating and recovering useful substances from exhaust gas generated during the treatment of the object to be treated including organic substances.
Moreover, since each grease filter is washed with washing water, the adsorption performance of useful materials by the grease filter is well maintained, which is more advantageous in efficiently separating and recovering useful materials from exhaust gas.
Moreover, since useful substances are recovered from the sewage obtained by washing the grease filter, it is advantageous in efficiently separating and recovering useful substances from the exhaust gas.
Further, among useful substances separated from the exhaust gas by the recovery unit, oil can be reused for fuel, paint and resin material, and ash can be reused as building aggregate and admixture.
In addition, the useful material that has been emulsified in the sewage is adsorbed and removed by the porous material in the filtration tank, so that filtered water that does not contain useful material can be obtained. Since it can be reused as cleaning water, it is advantageous in saving cleaning water.
実施の形態の排気分離装置の構成を示す説明図である。It is explanatory drawing which shows the structure of the exhaust gas separation apparatus of embodiment. 実施の形態の排気分離装置の構成を示す正面図である。It is a front view which shows the structure of the exhaust gas separation apparatus of embodiment. 実施の形態の排気分離装置の構成を示す平面図である。It is a top view which shows the structure of the exhaust gas separation apparatus of embodiment. (A)は排ガス処理部の正面断面図、(B)は(A)のB-B線断面図、(C)は(B)のC-C線断面図である。(A) is a front sectional view of the exhaust gas treatment section, (B) is a sectional view taken along line BB of (A), and (C) is a sectional view taken along line CC of (B). グリスフィルタの平面図である。It is a top view of a grease filter.
 次に本発明の実施の形態の排気分離装置について図面を参照して説明する。
 図1に示すように、排気分離装置12は、有機物を含む処理対象物を処理する処理装置10から排出される排ガスから有用物である油分や灰分を分離すると共に、有用物が分離されることで浄化された排ガスを排気として大気中に放出するものである。
 また、本明細書において、有機物を含む処理対象物とは、廃棄プラスチック、生ゴミなどに代表される有機物を含む廃棄物に限定されず、間伐材などの樹木、樹木の樹皮、藻類など様々な有機物を含むものとする。
 なお、本発明の排気分離装置12が適用される処理装置10は、有機物を含む処理対象物の処理により排ガスを発生するものであればよく、例えば、過熱水蒸気を用いて有機物を含む処理対象物を加熱して炭化させる過熱水蒸気炭化装置、あるいは、有機物を含む処理対象物を熱分解する燻焼式減容化処理装置、あるいは、有機物を含む処理対象物を焼却する焼却装置などの従来公知の様々な処理装置に本発明は適用可能である。
Next, an exhaust gas separation apparatus according to an embodiment of the present invention will be described with reference to the drawings.
As shown in FIG. 1, the exhaust separation device 12 separates useful oils and ash from exhaust gas discharged from the treatment device 10 that treats a processing object including organic matter, and the useful matter is separated. The exhaust gas purified by the above is discharged into the atmosphere as exhaust gas.
In addition, in this specification, the processing target containing organic matter is not limited to waste containing organic matter typified by waste plastic and garbage, but various kinds of trees such as thinned wood, bark of trees, algae, etc. It shall contain organic matter.
In addition, the processing apparatus 10 to which the exhaust gas separation apparatus 12 of the present invention is applied may be any apparatus that generates exhaust gas by processing a processing target including organic matter. For example, the processing target including organic matter using superheated steam is used. Conventionally known devices such as a superheated steam carbonization device that heats and carbonizes, a fire burning type volume reduction processing device that thermally decomposes a processing object containing organic matter, or an incineration device that incinerates a processing object containing organic matter The present invention can be applied to various processing apparatuses.
 排気分離装置12は、排ガス処理部14、第1の回収部16、第2の回収部18、ろ過槽20、供給部22、洗浄部24などを含んで構成されている。
 図1~図3に示すように、排ガス処理部14は、排気ファン26、ダクト28、複数のグリスフィルタ30、シャワーノズル32、シャワーポンプ34、上貯留槽36、下貯留槽38を備えている。
 排気ファン26は、処理装置10から排出される排ガスをダクト28を介して吸引し不図示の煙突に送出するものである。
 ダクト28は、排ガスが流れる流路Fを形成するものである。
 図2、図3、図4(A)~(C)に示すように、本実施の形態では、ダクト28は、水平方向に沿って延在する矩形板状の上壁2802と、上壁2802の長手方向の両側から下方に延在する一対の側壁2804と、上壁2802の長手方向の両端のうち排ガスの流れの上流側に位置する端部から下方に延在する上流端壁2806と、上壁2802の長手方向の両端のうち排ガスの流れの下流側に位置する端部から下方に延在する下流端壁2808とを備え、それら上壁2802、一対の側壁2804、上流端壁2806、下流端壁2808によって流路Fが形成されている。
 また、ダクト28の下部は閉塞されておらず、下方に開放された開口部2810となっている。
 図4(A)に示すように、上流端壁2806には、貫通孔2806Aが形成され、この貫通孔2806Aは管路2812を介して処理装置10に接続され、管路2812には風量調整用のダンパ(不図示)が設けられている。
 下流端壁2808には、貫通孔2808Aが形成され、この貫通孔2808Aは、管路2814を介して排気ファン26に接続され、管路2814には風量調整用のダンパ(不図示)が設けられている。
 したがって、排気ファン26が作動することにより、処理装置10から排出された排ガスは、管路2812を介してダクト28の流路Fを上流端壁2806側から下流端壁2808側に向かって流れ、管路2814から排気ファン26を介して煙突に導かれ、大気中に排出される。
The exhaust separation device 12 includes an exhaust gas treatment unit 14, a first recovery unit 16, a second recovery unit 18, a filtration tank 20, a supply unit 22, a cleaning unit 24, and the like.
As shown in FIGS. 1 to 3, the exhaust gas processing unit 14 includes an exhaust fan 26, a duct 28, a plurality of grease filters 30, a shower nozzle 32, a shower pump 34, an upper storage tank 36, and a lower storage tank 38. .
The exhaust fan 26 sucks the exhaust gas discharged from the processing apparatus 10 through the duct 28 and sends it to a chimney (not shown).
The duct 28 forms a flow path F through which exhaust gas flows.
As shown in FIGS. 2, 3, and 4A to 4C, in the present embodiment, the duct 28 includes a rectangular plate-like upper wall 2802 extending along the horizontal direction, and an upper wall 2802. A pair of side walls 2804 extending downward from both sides in the longitudinal direction of the upper wall 2802, an upstream end wall 2806 extending downward from an end located on the upstream side of the flow of exhaust gas among the longitudinal ends of the upper wall 2802, A downstream end wall 2808 extending downward from an end located on the downstream side of the exhaust gas flow of both ends in the longitudinal direction of the upper wall 2802, the upper wall 2802, a pair of side walls 2804, an upstream end wall 2806, A flow path F is formed by the downstream end wall 2808.
Moreover, the lower part of the duct 28 is not obstruct | occluded, but becomes the opening part 2810 open | released below.
As shown in FIG. 4A, a through hole 2806A is formed in the upstream end wall 2806, and this through hole 2806A is connected to the processing apparatus 10 through a pipe line 2812. A damper (not shown) is provided.
A through hole 2808A is formed in the downstream end wall 2808, and this through hole 2808A is connected to the exhaust fan 26 via a pipe line 2814. The pipe line 2814 is provided with a damper (not shown) for adjusting the air volume. ing.
Therefore, when the exhaust fan 26 operates, the exhaust gas discharged from the processing apparatus 10 flows through the flow path F of the duct 28 from the upstream end wall 2806 side to the downstream end wall 2808 side via the pipe line 2812. It is led from the pipe line 2814 to the chimney through the exhaust fan 26 and discharged into the atmosphere.
 図5に示すように、グリスフィルタ30は、フィルタ体3002と、一対の網3004と、枠部3006とを備えている。
 フィルタ体3002は、排ガスの有用物を吸着するものであり金属繊維から構成され、矩形板状を呈している。
 金属繊維は例えば綿状、織物状、あるいは、三次元網状体を呈している。
 本実施の形態では、このような金属繊維としてアルミニウムを用いており、耐久性の向上が図られているが、金属繊維として従来公知の様々な金属材料を用いたものが使用可能である。
 一対の網3004は、フィルタ体3002の厚さ方向の両面を覆うものであり、矩形状の金属網で構成されている。
 枠部3006は、フィルタ体3002と一対の金属網3004とが重ね合わされた状態を保持するものであり、フィルタ体3002および一対の金属網3004の外縁に沿って枠状に延在する金属板で構成されている。
As shown in FIG. 5, the grease filter 30 includes a filter body 3002, a pair of nets 3004, and a frame portion 3006.
The filter body 3002 adsorbs useful substances of exhaust gas, is composed of metal fibers, and has a rectangular plate shape.
The metal fiber has, for example, a cotton shape, a fabric shape, or a three-dimensional network.
In the present embodiment, aluminum is used as such a metal fiber, and durability is improved. However, metal fibers using various conventionally known metal materials can be used.
The pair of nets 3004 covers both surfaces of the filter body 3002 in the thickness direction, and is configured by a rectangular metal net.
The frame portion 3006 holds the filter body 3002 and the pair of metal nets 3004, and is a metal plate that extends in a frame shape along the outer edges of the filter body 3002 and the pair of metal nets 3004. It is configured.
 図2、図3に示すように、複数のグリスフィルタ30は、互いに平行して排ガスの流れる方向に沿って等間隔をおいて並べられ、不図示のブラケットを介してダクト28の内面に取着されており、本実施の形態では、9枚のグリスフィルタ30が設けられている。
 なお、グリスフィルタ30の数は排ガスに含まれる有用物の量に応じて適宜設定すればよい。
 各グリスフィルタ30の上縁はダクト28の上壁2802の内面に隙間なく当接しており、各グリスフィルタ30の上縁の両端に接続して上下に延在する一対の側縁はダクト28の一対の側壁2804の内面に隙間なく当接しており、後述するように各グリスフィルタ30の下部は、ダクト28の開口部2810を介して上貯留槽36に貯留されたグリスフィルタ30を洗浄後の汚水W2に浸漬された状態となっている。
 したがって、ダクト28内の流路Fは、ダクト28の上壁2802の内面と、一対の側壁2804の内面と、汚水W2の水面とで囲まれた空間で形成されることになる。言い換えると、流路Fは、ダクト28の底部を除く内面と、汚水W2の水面とで構成されている。
As shown in FIGS. 2 and 3, the plurality of grease filters 30 are arranged in parallel with each other at equal intervals along the direction in which the exhaust gas flows, and are attached to the inner surface of the duct 28 via a bracket (not shown). In the present embodiment, nine grease filters 30 are provided.
In addition, what is necessary is just to set the number of the grease filters 30 suitably according to the quantity of the useful substance contained in waste gas.
The upper edge of each grease filter 30 is in contact with the inner surface of the upper wall 2802 of the duct 28 without a gap, and a pair of side edges connected to both ends of the upper edge of each grease filter 30 and extending vertically are provided on the duct 28. A pair of side walls 2804 are in contact with the inner surfaces of the pair of side walls 2804 without any gap. As will be described later, the lower portion of each grease filter 30 is cleaned with the grease filter 30 stored in the upper storage tank 36 through the opening 2810 of the duct 28. It is in a state immersed in the sewage W2.
Therefore, the flow path F in the duct 28 is formed in a space surrounded by the inner surface of the upper wall 2802 of the duct 28, the inner surfaces of the pair of side walls 2804, and the water surface of the dirty water W2. In other words, the flow path F is comprised by the inner surface except the bottom part of the duct 28, and the water surface of the sewage W2.
 図3、図4(A)、(B)、(C)に示すように、シャワーノズル32は、ダクト28の内部で隣り合うグリスフィルタ30の間の空間にそれぞれ配置され、各グリスフィルタ30に向けて洗浄水W1を噴射することでグリスフィルタ30に吸着された有用物を洗浄するものである。
 また、シャワーノズル32から噴射された洗浄水W1は、グリスフィルタ30やダクト28の壁面(内面)に勢い良く衝突することでミストとなり、流路F内にミストが充満した状態となる。
 このようなミストが排ガス中の有用物を吸着して下方に落下することで排ガスの浄化効率の向上が図られている。
 また、ミストの発生を促進するために、シャワーノズル32から噴射された洗浄水W1が当たる箇所にミスト発生用の板体を設けるなど任意である。
 また、発生したミストを正または負に帯電させる帯電部を設け、有用物をより効率的にミストに吸着させるようにしてもよい。
 また、ミストは、ミストの粒径と同じ程度の粒径の物質を吸着する性質を有しており、ミストの粒径が小さいほど小さい物質を吸着することができる。
 したがって、排ガス中の有用物の粒径と同等の粒径のミストが生成されるように、シャワーノズル32のノズル径、洗浄水W1の噴射速度、噴射量などの条件を設定することが有用物を効率的にミストに吸着させる上で有利となる。
As shown in FIGS. 3, 4 (A), (B), and (C), the shower nozzle 32 is disposed in the space between the adjacent grease filters 30 inside the duct 28. The useful water adsorbed by the grease filter 30 is washed by spraying the washing water W1 toward the surface.
Moreover, the washing water W1 sprayed from the shower nozzle 32 becomes a mist by vigorously colliding with the grease filter 30 and the wall surface (inner surface) of the duct 28, and the flow path F is filled with the mist.
Such mist adsorbs useful substances in the exhaust gas and falls downward to improve the purification efficiency of the exhaust gas.
Moreover, in order to promote generation | occurrence | production of mist, it is arbitrary, such as providing the plate body for mist generation in the location where the washing water W1 injected from the shower nozzle 32 hits.
In addition, a charging unit that positively or negatively charges the generated mist may be provided so that useful substances can be more efficiently adsorbed to the mist.
Moreover, mist has the property to adsorb | suck the substance of a particle size comparable as the particle size of mist, and it can adsorb | suck a small substance, so that the particle size of mist is small.
Therefore, it is useful to set conditions such as the nozzle diameter of the shower nozzle 32, the injection speed of the cleaning water W1, and the injection amount so that a mist having a particle size equivalent to that of the useful material in the exhaust gas is generated. This is advantageous in efficiently adsorbing to the mist.
 シャワーポンプ34は、ろ過槽20に貯留された洗浄水W1を配管35(図2、図4(A)参照)を介して各シャワーノズル32に供給するものである。
 本実施の形態では、各シャワーノズル32とシャワーポンプ34が、各グリスフィルタ30に洗浄水W1を噴射することでグリスフィルタ30に吸着された有用物を洗浄する洗浄部24を構成すると共に、ダクト28内に水を噴射することでダクト28内にミストを発生させるミスト発生部として機能する。
The shower pump 34 supplies the cleaning water W1 stored in the filtration tank 20 to each shower nozzle 32 via a pipe 35 (see FIGS. 2 and 4A).
In the present embodiment, each shower nozzle 32 and shower pump 34 constitute a cleaning unit 24 that cleans useful materials adsorbed on the grease filter 30 by injecting cleaning water W1 to each grease filter 30, and a duct. It functions as a mist generating part that generates mist in the duct 28 by injecting water into the 28.
 図2、図3に示すように、上貯留槽36は、平面視した状態でダクト28の輪郭よりも大きな輪郭を有し水平方向に沿って延在する矩形板状の底壁3602と、底壁3602の長手方向の両側から起立する一対の側壁3604と、底壁3602の長手方向の両端から起立する一対の端壁3606とを備え、上貯留槽36の上部は開口部3608となっている。
 上貯留槽36は、その長手方向をダクト28の長手方向と合致させた状態で、開口部3608を介してダクト28の下部を収容し、ダクト28の下縁(一対の側壁2804、上流端壁2806、下流端壁2808の下縁)は、上貯留槽36の上縁(一対の側壁3604および一対の端壁3606の上縁)よりも下方に位置している。
 また、底壁3602の長手方向の一方寄りでダクト28の下流端壁2808の外側の箇所には、底壁3602の長手方向と直交しかつ一対の側壁3604間にわたって延在する仕切壁3610が上方に起立しており、仕切壁3610の上縁3610Aは、上貯留槽36の上縁より下方に位置している。
 仕切壁3610とこの仕切壁3610寄りの端壁3606との間に位置する底壁3602の部分には貫通孔3612が形成されている。
 したがって、シャワーノズル32から洗浄水がグリスフィルタ30に噴射されることでグリスフィルタ30から有用物を含む汚水が流下して上貯留槽36に貯留され、やがて上貯留槽36に貯留された汚水W2が仕切壁3610の上縁3610Aから溢れると、その汚水W2は底壁3602に流れ落ち、貫通孔3612を介して下方に流出する。
 ここで、図2に示すように、上貯留槽36に貯留される汚水W2の水面がグリスフィルタ30の下縁30Aよりも上方に位置するように仕切壁3610の上縁3610Aの高さを設定することで、グリスフィルタ30の下部は上貯留槽36に貯留された汚水W2に浸漬されることになる。
As shown in FIGS. 2 and 3, the upper storage tank 36 includes a rectangular plate-like bottom wall 3602 having a larger outline than the duct 28 in a plan view and extending in the horizontal direction, and a bottom. The wall 3602 includes a pair of side walls 3604 erected from both sides in the longitudinal direction and a pair of end walls 3606 erected from both ends of the bottom wall 3602 in the longitudinal direction. The upper portion of the upper storage tank 36 has an opening 3608. .
The upper storage tank 36 accommodates the lower part of the duct 28 through the opening 3608 in a state in which the longitudinal direction thereof coincides with the longitudinal direction of the duct 28, and the lower edge of the duct 28 (a pair of side walls 2804, an upstream end wall). 2806, the lower edge of the downstream end wall 2808) is located below the upper edge of the upper storage tank 36 (the upper edges of the pair of side walls 3604 and the pair of end walls 3606).
In addition, a partition wall 3610 extending perpendicularly to the longitudinal direction of the bottom wall 3602 and extending between the pair of side walls 3604 is located at a position nearer to the longitudinal direction of the bottom wall 3602 and outside the downstream end wall 2808 of the duct 28. The upper edge 3610A of the partition wall 3610 is positioned below the upper edge of the upper storage tank 36.
A through hole 3612 is formed in the portion of the bottom wall 3602 located between the partition wall 3610 and the end wall 3606 near the partition wall 3610.
Accordingly, the cleaning water is sprayed from the shower nozzle 32 to the grease filter 30, so that the sewage containing useful substances flows down from the grease filter 30 and is stored in the upper storage tank 36, and then the sewage W2 stored in the upper storage tank 36. When overflowing from the upper edge 3610A of the partition wall 3610, the sewage W2 flows down to the bottom wall 3602, and flows out downward through the through hole 3612.
Here, as shown in FIG. 2, the height of the upper edge 3610A of the partition wall 3610 is set so that the surface of the sewage W2 stored in the upper storage tank 36 is located above the lower edge 30A of the grease filter 30. By doing so, the lower part of the grease filter 30 is immersed in the sewage W2 stored in the upper storage tank 36.
 下貯留槽38は、上貯留槽36の下部に設けられ、下貯留槽38から貫通孔3612を介して流下する汚水W2を貯留するものである。
 下貯留槽38は、水平方向に沿って延在する矩形板状の底壁3802と、底壁3802の長手方向両側から起立する一対の側壁3804と、底壁3802の長手方向の両端から起立する一対の端壁3806とを備え、下貯留槽38の上部は上方に開放された開口部3808となっている。
 下貯留槽38は、上貯留槽36の貫通孔3612を含む底壁3602の大部分が下貯留槽38の開口部3808の内側に位置するように設けられている。
 また、2つの支持部材40が下貯留槽38の長手方向に間隔をおいて下貯留槽38の一対の側壁3804の上縁にわたって設けられており、これら2つの支持部材40によって上貯留槽386の底壁3802が支持されている。
 本実施の形態では、上貯留槽36および下貯留槽38が、洗浄水W1を噴射することで各グリスフィルタ30から流下する有用物を含む汚水W2を貯留する貯留槽を構成している。
The lower storage tank 38 is provided in the lower part of the upper storage tank 36, and stores the sewage W2 flowing down from the lower storage tank 38 through the through hole 3612.
The lower storage tank 38 stands from a rectangular plate-like bottom wall 3802 extending along the horizontal direction, a pair of side walls 3804 standing from both longitudinal sides of the bottom wall 3802, and both ends of the bottom wall 3802 in the longitudinal direction. A pair of end walls 3806 is provided, and the upper part of the lower storage tank 38 is an opening 3808 opened upward.
The lower storage tank 38 is provided so that most of the bottom wall 3602 including the through hole 3612 of the upper storage tank 36 is located inside the opening 3808 of the lower storage tank 38.
Further, two support members 40 are provided across the upper edges of the pair of side walls 3804 of the lower storage tank 38 at intervals in the longitudinal direction of the lower storage tank 38. A bottom wall 3802 is supported.
In this Embodiment, the upper storage tank 36 and the lower storage tank 38 comprise the storage tank which stores the waste water W2 containing the useful material which flows down from each grease filter 30 by injecting the wash water W1.
 なお、貯留槽を単一としてもよいが、本実施の形態のようにすると、各グリスフィルタ30から汚水W2が流下することで、汚水W2が激しく撹拌されている上貯留槽36と、汚水W2の流れが緩やかな下貯留槽38とを分離できるため、下貯留槽38において汚水W2の水面に有用物を浮上させやすくなり、後述する第1の回収部16による有用物の回収をより効率的に行なう上で有利となる。 In addition, although it is good also as a single storage tank, when it carries out like this Embodiment, when the waste water W2 flows down from each grease filter 30, the upper storage tank 36 in which the waste water W2 is stirred vigorously, and the waste water W2 Since the lower storage tank 38 can be separated from the lower storage tank 38, it becomes easier to float useful materials on the surface of the sewage W2 in the lower storage tank 38, and the collection of useful objects by the first recovery unit 16 described later is more efficient. It is advantageous in carrying out.
 図1に示すように、第1の回収部16は、下貯留槽38に貯留された汚水W2の上澄みを吸引して汚水W2から有用物を回収し残った汚水W2を下貯留槽38に戻すことで下貯留槽38内で汚水W2を循環させるものである。
 なお、図2、図3において第1の回収部16の図示は省略している。
 このような第1の回収部16として、例えば、株式会社寺田ポンプ製作所の浮上油回収装置(型番DS1-120)などの市販品を用いることができる。
 本実施の形態では、第1の回収部16は、コンプレッサ17を含んで構成されている。
 コンプレッサ17は、下貯留槽38に貯留された汚水W2に空気を注入するものである。
 コンプレッサ17により汚水W2に空気を注入することで、水よりも比重が大きい有用物に気泡を付着させて汚水W2の水面に浮上させることにより、水よりも比重が大きい有用物の回収を行なう上で有利となる。
 後述するように、有用物が炭化水素の割合が高い油分である場合、炭化水素は水に溶けず有用物の比重は水よりも大きくなるため、このような炭化水素の割合が高い油分を有用物として回収する場合に有利となる。
 第1の回収部16は、汚水W2の水面に浮上した有用物を回収するが、汚水W2の水面に浮上せずに汚水W2に混じった有用物、および、汚水W2にエマルジョン化して溶け込んだ有用物は回収できない。
As shown in FIG. 1, the first recovery unit 16 sucks the supernatant of the sewage W2 stored in the lower storage tank 38, recovers useful materials from the sewage W2, and returns the remaining sewage W2 to the lower storage tank 38. Thus, the sewage W2 is circulated in the lower storage tank 38.
2 and 3, the first collection unit 16 is not shown.
As such a first recovery unit 16, for example, a commercially available product such as a floating oil recovery device (model number DS1-120) of Terada Pump Manufacturing Co., Ltd. can be used.
In the present embodiment, the first recovery unit 16 includes a compressor 17.
The compressor 17 injects air into the sewage W2 stored in the lower storage tank 38.
By injecting air into the sewage W2 by the compressor 17, bubbles are attached to a useful substance having a specific gravity greater than that of water and floated on the surface of the sewage W2, thereby recovering the useful substance having a specific gravity greater than that of water. Is advantageous.
As will be described later, when useful substances are oils with a high proportion of hydrocarbons, hydrocarbons do not dissolve in water and the specific gravity of useful substances is greater than that of water, so oils with a high proportion of such hydrocarbons are useful. This is advantageous when recovered as a product.
The first recovery unit 16 recovers useful materials that have floated on the surface of the sewage W2, but does not float on the surface of the sewage W2, and is useful that has been emulsified and dissolved in the sewage W2. Things cannot be recovered.
 図1に示すように、第2の回収部18は、下貯留槽38に貯留される汚水W2の水面よりも下方、あるいは、下貯留槽38の底壁3802近傍に位置する汚水W2から有用物を回収し残った汚水W2を排出するものである。
 本実施の形態では、図2、図3に示すように、下貯留槽38の底壁3802上に第1の送りポンプ42を設け、下貯留槽38の汚水W2の水面よりも下方に位置する汚水W2を第1の送りポンプ42および配管43を介して第2の回収部18に給送している。
 第2の回収部18として例えば以下のような原理のものが使用できる。
 水平方向に延在する軸心を有する円筒形のフィルタ1802をモータ1804により一方向に回転させつつ、フィルタ1802の半径方向外側から半径方向内側に汚水W2を通過させてフィルタ1802の外周面に汚水W2に含まれる有用物を付着させる。
 このフィルタ1802と平行する軸心を有し、フィルタ1802の外周面に当接する円筒面を有する転写ロール1806をフィルタ1802に接触させ、その接触状態を維持しつつ転写ロール1806をフィルタ1802の回転に従動回転させ、フィルタ1802の外周面の有用物を転写ロール1806の外周面に付着させる。
 転写ロール1806の外周面にドクター1808の先部を接触させドクター1808により転写ロール1806の外周面から有用物を掻き取ることで有用物を回収する。
 一方、フィルタ1802を通過した汚水W2は、第2の回収部18から排出される。
 このような第2の回収部18として、例えば、株式会社サトミ製作所の商品名新型エコフィルターなどの市販品を用いることができる。
 また、本実施の形態では、フィルタ1802を光触媒材料(例えば酸化チタン)で形成されたメッシュで構成すると共に、フィルタ1802に向けて紫外線を照射する紫外線光源1810を設けている。
 そのため、紫外線が照射されることにより活性化されたフィルタ1802(光触媒材料)によって汚水W2に含まれる化学物質が分解されるため、汚水W2に含まれる例えば有害な化学物質の無害化が図られ、汚水W2の浄化を図る上で有利となっている。
 したがって、第2の回収部18は、光触媒材料と紫外線光とを用いて汚水W2に含まれる化学物質を分解処理する光触媒処理部19を含んで構成され、光触媒処理部19は、フィルタ1802と紫外線光源1810とにより構成されている。
 なお、光触媒処理部19は、汚水W2に含まれる化学物質を光触媒材料を用いて分解処理できればよく、フィルタ1802と別体に設けた光触媒材料に紫外線を照射しつつ汚水W2を接触させるなど従来公知の様々な構成が採用可能である。
 第2の回収部18は、汚水W2の水面に浮上せずに汚水W2に混じった有用物を回収するが、汚水W2にエマルジョン化して溶け込んだ有用物は回収できない。
As shown in FIG. 1, the second recovery unit 18 is useful from sewage W2 located below the surface of the sewage W2 stored in the lower storage tank 38 or near the bottom wall 3802 of the lower storage tank 38. The remaining sewage W2 is discharged.
In the present embodiment, as shown in FIGS. 2 and 3, the first feed pump 42 is provided on the bottom wall 3802 of the lower storage tank 38, and is positioned below the water surface of the sewage W <b> 2 in the lower storage tank 38. The sewage W2 is fed to the second recovery unit 18 via the first feed pump 42 and the pipe 43.
For example, the following principle can be used as the second recovery unit 18.
A cylindrical filter 1802 having an axial center extending in the horizontal direction is rotated in one direction by a motor 1804, and the sewage W2 is passed from the radially outer side to the radially inner side of the filter 1802 so that the outer surface of the filter 1802 has The useful substance contained in W2 is adhered.
A transfer roll 1806 having an axial center parallel to the filter 1802 and having a cylindrical surface that contacts the outer peripheral surface of the filter 1802 is brought into contact with the filter 1802, and the transfer roll 1806 is rotated by the filter 1802 while maintaining the contact state. Following rotation, useful materials on the outer peripheral surface of the filter 1802 are attached to the outer peripheral surface of the transfer roll 1806.
The tip of the doctor 1808 is brought into contact with the outer peripheral surface of the transfer roll 1806 and the useful material is collected by scraping the useful material from the outer peripheral surface of the transfer roll 1806 by the doctor 1808.
On the other hand, the sewage W2 that has passed through the filter 1802 is discharged from the second recovery unit 18.
As such 2nd collection | recovery part 18, commercial items, such as a brand name new type eco filter of Satomi Manufacturing Co., Ltd., can be used, for example.
In this embodiment mode, the filter 1802 is formed using a mesh formed of a photocatalytic material (eg, titanium oxide), and an ultraviolet light source 1810 that irradiates ultraviolet light toward the filter 1802 is provided.
Therefore, the chemical substance contained in the sewage W2 is decomposed by the filter 1802 (photocatalyst material) activated by irradiating ultraviolet rays, and thus, for example, harmful chemical substances contained in the sewage W2 are detoxified. This is advantageous in purifying the sewage W2.
Therefore, the second recovery unit 18 includes a photocatalyst processing unit 19 that decomposes a chemical substance contained in the sewage W2 using a photocatalyst material and ultraviolet light. The photocatalyst processing unit 19 includes the filter 1802 and the ultraviolet light. And a light source 1810.
The photocatalyst processing unit 19 only needs to be able to decompose the chemical substance contained in the sewage W2 by using a photocatalyst material, and conventionally known such as contacting the sewage W2 while irradiating the photocatalyst material provided separately from the filter 1802 with ultraviolet light Various configurations can be adopted.
The second recovery unit 18 recovers useful materials mixed in the sewage W2 without floating on the surface of the sewage W2, but cannot recover useful materials that are emulsified and dissolved in the sewage W2.
 図1に示すように、ろ過槽20は、有用物を吸着する多孔質材料(不図示)が収容され第2の回収部18から排出される汚水W2から多孔質材料によって有用物を吸着することで汚水W2のろ過を行ないろ過水を生成するものである。
 本実施の形態では、図1、図2に示すように、第2の回収部18から排出された汚水W2は、第2の送りポンプ44、不図示の配管を介してろ過槽20に給送され、汚水W2はろ過槽20に貯留される。
 多孔質材料として、例えば、雪ヶ谷化学工業株式会社の微生物固定化PVA(Polyvinyl Alcohol)担体(ポリビニールアルコール担体)である商品名Y-CUBEなどの市販品が使用可能である。
 ろ過槽20では、汚水W2にエマルジョン化して溶け込んだ有用物が多孔質材料によって吸着されることで有用物が取り除かれたろ過水が得られる。
As shown in FIG. 1, the filtration tank 20 contains a porous material (not shown) that adsorbs a useful material and adsorbs the useful material from the sewage W2 discharged from the second recovery unit 18 by the porous material. Then, the sewage W2 is filtered to produce filtered water.
In the present embodiment, as shown in FIGS. 1 and 2, the sewage W2 discharged from the second recovery unit 18 is fed to the filtration tank 20 via the second feed pump 44 and a pipe (not shown). The sewage W2 is stored in the filtration tank 20.
As the porous material, for example, a commercially available product such as Y-CUBE, which is a microorganism-immobilized PVA (Polyvinyl Alcohol) carrier (polyvinyl alcohol carrier) of Yukigaya Chemical Co., Ltd., can be used.
In the filtration tank 20, the useful material that has been emulsified and dissolved in the sewage W <b> 2 is adsorbed by the porous material, so that filtered water from which the useful material has been removed is obtained.
 供給部22は、ろ過槽20で生成されたろ過水を洗浄水W1としてろ過槽20から洗浄部24に供給するものであり、本実施の形態では、供給部22はシャワーポンプ34で構成されている。 The supply unit 22 supplies the filtered water generated in the filtration tank 20 as the cleaning water W1 from the filtration tank 20 to the cleaning unit 24. In the present embodiment, the supply unit 22 includes a shower pump 34. Yes.
 洗浄部24は、ろ過槽20に貯留されたろ過水に空気を注入することで多孔質材料の洗浄を行なうものであり、例えば、ポンプやコンプレッサなどで構成されている。
 多孔質材料の洗浄は所定時間毎に実施され、この際、ろ過水によって多孔質材料を洗浄することで汚れた、言い換えると、有用物で汚れたろ過水は、第3の送りポンプ46によって第2の回収部18に給送される。
 そのため、多孔質材料に吸着されていた有用物が第2の回収部18によって分離回収される。
 本実施の形態では、第3の送りポンプ46が、洗浄部24による多孔質材料の洗浄により汚れたろ過水を第2の回収部18に給送する給送部を構成している。
The washing | cleaning part 24 wash | cleans a porous material by inject | pouring air into the filtered water stored in the filtration tank 20, for example, is comprised with a pump, a compressor, etc.
The porous material is cleaned every predetermined time. At this time, the porous material is contaminated by washing the porous material with filtered water. 2 to the collecting unit 18.
Therefore, the useful substance adsorbed on the porous material is separated and recovered by the second recovery unit 18.
In the present embodiment, the third feed pump 46 constitutes a feed unit that feeds filtered water contaminated by the cleaning of the porous material by the cleaning unit 24 to the second recovery unit 18.
 なお、排気分離装置12において洗浄水W1、ろ過水、汚水W2が循環するためには、予めろ過槽20、上貯留槽36、下貯留槽38に所定量の水を貯留しておくことが必要である。
 また、排ガスに含まれる水分がグリスフィルタ30を洗浄する洗浄水W1に吸着されることで、排気分離装置12を循環する水の総量が時間経過と共に増加するが、増加した水は適宜排出すればよい。
 例えば、ろ過槽20に貯留される水が規定量を超えた場合に規定量を超えたろ過水を排出すればよい。
In order to circulate the cleaning water W1, filtered water, and sewage W2 in the exhaust separation device 12, it is necessary to store a predetermined amount of water in the filtration tank 20, the upper storage tank 36, and the lower storage tank 38 in advance. It is.
Further, the amount of water contained in the exhaust gas is adsorbed by the cleaning water W1 for cleaning the grease filter 30, so that the total amount of water circulating in the exhaust separation device 12 increases with the passage of time. Good.
For example, when the water stored in the filtration tank 20 exceeds a specified amount, the filtered water exceeding the specified amount may be discharged.
 次に作用効果について説明する。
 処理装置10から排出された排ガスが複数のグリスフィルタ30を通過すると排ガスの有用物が複数のグリスフィルタ30によって効率的に吸着されるため、臭気の少ない環境に影響を与えない排気を行なうことができることは無論のこと、有機物を含む処理対象物の処理に伴って発生する排ガスから有用物を効率的に分離回収する上で有利となる。
 また、各グリスフィルタ30は洗浄水W1によって洗浄されるため、グリスフィルタ30による有用物の吸着性能が良好に維持されるため、排ガスから有用物を効率的に分離回収する上でより有利となる。
 また、グリスフィルタ30を洗浄することで得られた第2の貯留槽38に貯留された汚水W2から有用物を回収するようにしたので、排ガスから有用物を効率的に分離回収する上で有利となる。
 また、本実施の形態では、第1の回収部16により第2の貯留槽38に貯留された汚水W2の上澄みを吸引して汚水W2から有用物を回収し残った汚水W2を第2の貯留槽38に戻すことで第2の貯留槽38内で汚水W2を循環させると共に、第2の回収部18により第2の貯留槽38に貯留される汚水W2のうち上澄みよりも下方に位置する汚水W2から有用物を回収し残った汚水W2を排出するようにした。
 したがって、汚水W2の水面に浮上する有用物と、汚水W2の水面に浮上しにくい有用物との双方を確実に回収でき、排ガスから有用物を効率的に分離回収する上でより有利となる。
 また、第1、第2の回収部16、18により排ガスから分離された有用物のうち油分は、燃料、塗料、樹脂材料に再利用でき、灰分は建築用の骨材、混和剤として再利用することができ、排ガスから分離回収した有用物を資源として使用することができる。
 また、汚水W2に含まれるエマルジョン化した有用物はろ過槽20において多孔質材料によって吸着され取り除かれることで有用物を含まないろ過水を得ることができ、このような清浄なろ過水をグリスフィルタ30を洗浄する洗浄水W1として再利用できるため、洗浄水W1の節約を図る上で有利となる。
Next, the function and effect will be described.
When the exhaust gas discharged from the processing apparatus 10 passes through the plurality of grease filters 30, the exhaust gas useful substances are efficiently adsorbed by the plurality of grease filters 30, so that exhaust without affecting the environment with less odor can be performed. Needless to say, this is advantageous in efficiently separating and recovering useful substances from the exhaust gas generated during the treatment of the object to be treated including organic substances.
In addition, since each grease filter 30 is washed with the washing water W1, the adsorption performance of useful materials by the grease filter 30 is maintained well, which is more advantageous in efficiently separating and recovering useful materials from exhaust gas. .
Moreover, since useful substances are recovered from the sewage W2 stored in the second storage tank 38 obtained by cleaning the grease filter 30, it is advantageous in efficiently separating and recovering useful substances from the exhaust gas. It becomes.
Further, in the present embodiment, the first collection unit 16 sucks the supernatant of the sewage W2 stored in the second storage tank 38 to collect useful materials from the sewage W2 and stores the remaining sewage W2 in the second storage. The sewage W2 is circulated in the second storage tank 38 by returning to the tank 38, and the sewage W2 stored in the second storage tank 38 by the second recovery unit 18 is located below the supernatant. The useful material was recovered from W2 and the remaining sewage W2 was discharged.
Therefore, it is possible to reliably collect both useful materials that float on the surface of the sewage W2 and useful materials that do not easily float on the surface of the sewage W2, which is more advantageous in efficiently separating and recovering useful materials from the exhaust gas.
Of the useful materials separated from the exhaust gas by the first and second recovery units 16 and 18, oil can be reused as fuel, paint, resin material, and ash can be reused as building aggregate and admixture. The useful material separated and recovered from the exhaust gas can be used as a resource.
Further, the emulsified useful material contained in the sewage W2 is adsorbed and removed by the porous material in the filtration tank 20, so that filtered water containing no useful material can be obtained, and such clean filtered water is used as a grease filter. 30 can be reused as cleaning water W1 for cleaning, which is advantageous for saving the cleaning water W1.
 また、本実施の形態では、ダクト28内に洗浄水W1を噴射することでダクト28内に発生したミストに有用物を吸着させることができるため、排ガスから有用物を効率的に分離する上でより有利となる。
 また、本実施の形態では、グリスフィルタ30の下部を貯留槽に貯留された汚水W2に浸漬させることで、ダクト28の底部を汚水W2で形成したが、ダクト28の底壁を別途設けても良い。この場合は、ダクト28内の負圧を維持しつつダクト28の底壁3802から汚水W2を排出する構成を設ければよい。
 しかしながら、本実施の形態のようにすると、ダクト28内の負圧を維持する構成を設ける必要がなく、ダクト28の構成の簡素化、コンパクト化を図る上で有利となる。
 また、本実施の形態では、ろ過槽20に貯留された汚水W2に空気を注入することで多孔質材料の洗浄を行なうようにしたので、多孔質材料の洗浄に要する設備を最小限にでき、設備費用の抑制を図る上で有利となる。
 また、多孔質材料の洗浄により汚れたろ過水を第2の回収部18に供給することでさらに有用物を分離回収できるため、排ガスから有用物を効率的に分離する上でより有利となる。
Moreover, in this Embodiment, since a useful substance can be made to adsorb | suck to the mist which generate | occur | produced in the duct 28 by injecting the washing water W1 in the duct 28, when separating a useful substance from waste gas efficiently. More advantageous.
Moreover, in this Embodiment, the bottom part of the duct 28 was formed with the sewage W2 by immersing the lower part of the grease filter 30 in the sewage W2 stored in the storage tank, but the bottom wall of the duct 28 may be provided separately. good. In this case, a configuration for discharging the sewage W2 from the bottom wall 3802 of the duct 28 while maintaining the negative pressure in the duct 28 may be provided.
However, according to the present embodiment, there is no need to provide a configuration for maintaining the negative pressure in the duct 28, which is advantageous in simplifying the configuration of the duct 28 and achieving compactness.
In the present embodiment, since the porous material is washed by injecting air into the sewage W2 stored in the filtration tank 20, the equipment required for washing the porous material can be minimized, This is advantageous for reducing equipment costs.
Further, since the useful material can be further separated and recovered by supplying the filtered water contaminated by the cleaning of the porous material to the second recovery unit 18, it is more advantageous in efficiently separating the useful material from the exhaust gas.
 ここで、排ガスから分離される有用物のうち油分について説明する。
 有機物を含む処理対象物を燃焼して処理する焼却装置においては、焼却された有機物は炭に変化し、発生する排気ガス(煙)には、水、灰分が含まれている。
 また、有機物を含む処理対象物を炭化処理する過熱水蒸気炭化装置においては、有機物は炭化すると共に、発生する排気ガス(煙)には、水、乾留ガス、僅かな油分が含まれている。
 また、有機物を含む処理対象物を熱分解する燻焼式減容化処理装置においては、処理された有機物がセラミック(灰)に変化すると共に、発生する排気ガス(煙)には、水、乾留ガス、不純物を含む油分が含まれる。
 なお、乾留ガスは一酸化炭素などの燃焼ガスを含んでいるため、その燃焼ガスを燃料として使用することができる。
Here, the oil content among useful substances separated from the exhaust gas will be described.
In an incinerator that burns and treats a processing object containing organic matter, the incinerated organic matter changes to charcoal, and the generated exhaust gas (smoke) contains water and ash.
Moreover, in the superheated steam carbonization apparatus which carbonizes the process target object containing organic substance, while organic substance carbonizes, the generated exhaust gas (smoke) contains water, dry distillation gas, and a slight oil component.
In addition, in the smoldering type volume reduction processing equipment that thermally decomposes the processing object containing organic matter, the treated organic matter changes to ceramic (ash) and the generated exhaust gas (smoke) includes water, dry distillation Gas and oil containing impurities are included.
Since the dry distillation gas contains a combustion gas such as carbon monoxide, the combustion gas can be used as a fuel.
 例えば、燻焼式減容化処理装置の排気ガスから本実施の形態の排気分離装置12を用いて回収した油分に含まれる炭化水素の割合は、一般的な原油並となり、原油に相当する熱量を有する油分を有用物として回収することが可能となっている。
 したがって、処理装置10として、燻焼式減容化処理装置を使用する場合、本実施の形態の排気分離装置12を用いることで、有用物として原油に相当する油分を効率よく回収する上で極めて有利となっている。
 さらに、処理対象物として、コストが安価で、かつ、炭化水素を多く含む廃棄プラスチック、間伐材、樹皮などを燻焼式減容化処理装置で処理すると、原油に相当する油分をより効率的に回収することができ、安価で高付加価値の有用物を得る上で有利となる。
For example, the ratio of hydrocarbons contained in the oil recovered from the exhaust gas of the smoldering type volume reduction processing apparatus using the exhaust separation device 12 of the present embodiment is the same as that of general crude oil, and the amount of heat corresponding to crude oil. It is possible to collect the oil component having a useful product.
Therefore, when a smoldering type volume reduction processing apparatus is used as the processing apparatus 10, it is extremely difficult to efficiently collect oil corresponding to crude oil as a useful product by using the exhaust separation apparatus 12 of the present embodiment. It is advantageous.
Furthermore, if waste plastics, thinned wood, bark, etc., which are low in cost and contain a large amount of hydrocarbons, are treated with a fire burning type volume reduction treatment device, the oil equivalent to crude oil is more efficiently treated. It can be recovered and is advantageous in obtaining a cheap and high value-added useful product.
10 処理装置
12 排気分離装置
14 排ガス処理部
16 第1の回収部(回収部)
17 コンプレッサ
18 第2の回収部(回収部)
19 光触媒処理部
20 ろ過槽
22 供給部
24 洗浄部
26 排気ファン
28 ダクト
2810 開口部
30 グリスフィルタ
32 シャワーノズル
34 シャワーポンプ
36 上貯留槽(貯留槽)
38 下貯留槽(貯留槽)
46 第3の送りポンプ(給送部)
F 流路
DESCRIPTION OF SYMBOLS 10 Processing apparatus 12 Exhaust gas separation apparatus 14 Exhaust gas processing part 16 1st collection | recovery part (collection part)
17 Compressor 18 Second recovery unit (recovery unit)
DESCRIPTION OF SYMBOLS 19 Photocatalyst processing part 20 Filtration tank 22 Supply part 24 Washing part 26 Exhaust fan 28 Duct 2810 Opening part 30 Grease filter 32 Shower nozzle 34 Shower pump 36 Upper storage tank (storage tank)
38 Lower storage tank (storage tank)
46 Third feed pump (feeding section)
F channel

Claims (8)

  1.  有用物を含む排ガスから前記有用物を分離する排気分離装置であって、
     前記排ガスが流れる流路を形成するダクトと、
     前記ダクト内に、前記排ガスの流れる方向に間隔をおいて並べられた、前記有用物を吸着する複数のグリスフィルタと、
     前記各グリスフィルタに洗浄水を噴射することで前記グリスフィルタに吸着された前記有用物を洗浄する洗浄部と、
     前記洗浄水を噴射することで前記各グリスフィルタから流下する前記有用物を含む汚水を貯留する貯留槽と、
     前記貯留槽に貯留された前記汚水から前記有用物を回収し残った前記汚水を排出する回収部と、
     前記有用物を吸着する多孔質材料が収容され前記回収部から排出される前記汚水から前記多孔質材料によって前記有用物を吸着することで前記汚水のろ過を行ないろ過水を生成するろ過槽と、
     前記ろ過水を前記洗浄水として前記ろ過槽から前記洗浄部に供給する供給部と、
     を備えることを特徴とする排気分離装置。
    An exhaust separation device for separating the useful material from exhaust gas containing the useful material,
    A duct forming a flow path through which the exhaust gas flows;
    A plurality of grease filters that adsorb the useful substances arranged in the duct at intervals in the flow direction of the exhaust gas,
    A cleaning unit for cleaning the useful matter adsorbed on the grease filter by spraying cleaning water on each grease filter;
    A storage tank for storing sewage containing the useful material flowing down from each grease filter by spraying the washing water;
    A collection unit that collects the useful material from the sewage stored in the storage tank and discharges the remaining sewage;
    A filtration tank that contains the porous material that adsorbs the useful material and that filters the waste water by adsorbing the useful material from the sewage discharged from the recovery unit by the porous material to generate filtered water;
    A supply unit for supplying the filtered water as the washing water from the filtration tank to the washing unit;
    An exhaust gas separation device comprising:
  2.  前記洗浄部は、前記ダクト内に前記洗浄水を噴射することで前記ダクト内にミストを発生させるミスト発生部として機能する、
     ことを特徴とする請求項1記載の排気分離装置。
    The cleaning unit functions as a mist generating unit that generates mist in the duct by injecting the cleaning water into the duct.
    The exhaust gas separation apparatus according to claim 1.
  3.  前記ダクトの底部は前記貯留槽に開口しており、
     前記グリスフィルタの下部が前記貯留槽に貯留された前記汚水に浸漬され、
     前記流路は、前記ダクトの前記底部を除く内面と、前記汚水の水面とで構成されている、
     ことを特徴とする請求項1または2記載の排気分離装置。
    The bottom of the duct is open to the storage tank,
    The lower part of the grease filter is immersed in the sewage stored in the storage tank,
    The flow path is composed of an inner surface excluding the bottom of the duct and a water surface of the sewage,
    The exhaust gas separation apparatus according to claim 1 or 2, wherein
  4.  前記回収部は、
     前記貯留槽に貯留された前記汚水の上澄みを吸引して前記汚水から前記有用物を回収し残った前記汚水を前記貯留槽に戻すことで前記貯留槽内で前記汚水を循環させる第1の回収部と、
     前記貯留槽に貯留される前記汚水のうち上澄みよりも下方に位置する前記汚水から前記有用物を回収し残った前記汚水を排出する第2の回収部と、
     を備えることを特徴とする請求項1から3の何れか1項記載の排気分離装置。
    The collection unit
    1st collection | recovery which circulates the said sewage in the said storage tank by attracting | sucking the supernatant of the said sewage stored in the said storage tank, collect | recovering the said useful materials from the said sewage, and returning the remaining sewage to the said storage tank And
    A second recovery unit that discharges the remaining sewage from the sewage stored in the storage tank from the sewage located below the supernatant;
    The exhaust gas separation device according to any one of claims 1 to 3, further comprising:
  5.  前記第1の回収部は、前記貯留槽に貯留された前記汚水に空気を注入するコンプレッサを備える、
     ことを特徴とする請求項4記載の排気分離装置。
    The first recovery unit includes a compressor that injects air into the sewage stored in the storage tank,
    The exhaust gas separation apparatus according to claim 4.
  6.  前記第2の回収部は、光触媒材料と紫外線光とを用いて前記汚水に含まれる化学物質を分解処理する光触媒処理部を備える、
     ことを特徴とする請求項4または5記載の排気分離装置。
    The second recovery unit includes a photocatalyst processing unit that decomposes a chemical substance contained in the sewage using a photocatalytic material and ultraviolet light.
    The exhaust gas separation apparatus according to claim 4 or 5, characterized by the above.
  7.  前記ろ過槽に貯留された前記ろ過水に空気を注入することで前記多孔質材料の洗浄を行なう洗浄部をさらに備える、
     ことを特徴とする請求項1から6の何れか1項記載の排気分離装置。
    A cleaning unit for cleaning the porous material by injecting air into the filtered water stored in the filtration tank;
    The exhaust gas separation device according to any one of claims 1 to 6, wherein
  8.  前記洗浄部による前記多孔質材料の洗浄により汚れた前記ろ過水を前記回収部に給送する給送部をさらに備える、
     ことを特徴とする請求項7記載の排気分離装置。
    A feed unit that feeds the filtered water contaminated by the washing of the porous material by the washing unit to the recovery unit;
    The exhaust gas separation apparatus according to claim 7.
PCT/JP2018/008267 2017-03-23 2018-03-05 Exhaust separation device WO2018173714A1 (en)

Applications Claiming Priority (4)

Application Number Priority Date Filing Date Title
JP2017-057503 2017-03-23
JP2017057503 2017-03-23
JP2017151277A JP2018158329A (en) 2017-03-23 2017-08-04 Exhaust separation device
JP2017-151277 2017-08-04

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS621431A (en) * 1985-06-25 1987-01-07 株式会社 道前築炉工業 Oil recovery device for high-molecular solid waste carbonized gas
JPH10165864A (en) * 1996-12-12 1998-06-23 Nippon Paint Plant Eng Kk Coating device for water-base paint
JP2004017040A (en) * 2002-06-17 2004-01-22 Koichi Nishio Recovery apparatus for included powder
CN104606964A (en) * 2013-11-01 2015-05-13 上海汉宝净化专业技术有限公司 Oil smoke separating smell-removing device
JP3212759U (en) * 2017-07-20 2017-09-28 株式会社サトミ製作所 Smoke removal equipment

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS621431A (en) * 1985-06-25 1987-01-07 株式会社 道前築炉工業 Oil recovery device for high-molecular solid waste carbonized gas
JPH10165864A (en) * 1996-12-12 1998-06-23 Nippon Paint Plant Eng Kk Coating device for water-base paint
JP2004017040A (en) * 2002-06-17 2004-01-22 Koichi Nishio Recovery apparatus for included powder
CN104606964A (en) * 2013-11-01 2015-05-13 上海汉宝净化专业技术有限公司 Oil smoke separating smell-removing device
JP3212759U (en) * 2017-07-20 2017-09-28 株式会社サトミ製作所 Smoke removal equipment

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