Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP6890318B2 - Dust removal system and dust removal method - Google Patents
[go: Go Back, main page]

JP6890318B2 - Dust removal system and dust removal method - Google Patents

Dust removal system and dust removal method Download PDF

Info

Publication number
JP6890318B2
JP6890318B2 JP2017082293A JP2017082293A JP6890318B2 JP 6890318 B2 JP6890318 B2 JP 6890318B2 JP 2017082293 A JP2017082293 A JP 2017082293A JP 2017082293 A JP2017082293 A JP 2017082293A JP 6890318 B2 JP6890318 B2 JP 6890318B2
Authority
JP
Japan
Prior art keywords
gas
dust
heat exchanger
heat
dust removal
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
JP2017082293A
Other languages
Japanese (ja)
Other versions
JP2018176103A (en
Inventor
亮 中久保
亮 中久保
陽一郎 小島
陽一郎 小島
三佳 石田
三佳 石田
弘一 天羽
弘一 天羽
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
National Agriculture and Food Research Organization
Original Assignee
National Agriculture and Food Research Organization
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by National Agriculture and Food Research Organization filed Critical National Agriculture and Food Research Organization
Priority to JP2017082293A priority Critical patent/JP6890318B2/en
Publication of JP2018176103A publication Critical patent/JP2018176103A/en
Application granted granted Critical
Publication of JP6890318B2 publication Critical patent/JP6890318B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Landscapes

  • Separation Of Particles Using Liquids (AREA)
  • Fertilizers (AREA)

Description

本発明は、気体中の潜熱を有効利用する技術に関し、気体中に含まれる粉塵の除去に関するものである。特に、堆肥化処理において発生する発酵熱を利用して堆肥化装置の排気中に含まれる粉塵を除去するものである。 The present invention relates to a technique for effectively utilizing latent heat in a gas, and to remove dust contained in the gas. In particular, the heat of fermentation generated in the composting process is used to remove dust contained in the exhaust gas of the composting apparatus.

有機物の堆肥化では一般的に有機物1kgあたり灯油550g相当(20MJ)の発酵熱が発生する。例えば、養豚の場合、日本の年間排せつ量788万t/年から灯油2.6万kL/年に相当する発酵熱が発生する。しかし、現状では発生した発酵熱が未利用のまま大気中へ排出されており、堆肥化において生じる発酵熱を有効利用するための研究が行われている。発酵熱の回収方法には、堆肥から熱を直接抽出する方法や熱を排気として回収する方法がある。後者の方法で回収される発酵熱は、主に、堆肥化装置からの排気が流れる通路に設置される熱交換器を介して水や空気の加温に利用される。出願人は、発酵熱によって加温された水(温水)を搾乳牛の飲用水に利用することによる乳量増加や、該温水を分娩豚舎の床暖房熱源に利用することによる暖房費削減といった発酵熱活用による経済的メリットを実証しつつある。 In composting organic matter, fermentation heat equivalent to 550 g (20 MJ) of kerosene is generally generated per 1 kg of organic matter. For example, in the case of pig farming, fermentation heat equivalent to kerosene 26,000 kL / year is generated from the annual excretion amount of 7.88 million tons / year in Japan. However, at present, the generated fermentation heat is discharged into the atmosphere without being used, and research is being conducted to effectively utilize the fermentation heat generated in composting. Fermentation heat recovery methods include a method of directly extracting heat from compost and a method of recovering heat as exhaust gas. The heat of fermentation recovered by the latter method is mainly used for heating water and air via a heat exchanger installed in the passage through which the exhaust from the composting apparatus flows. The applicant can increase the milk yield by using the water heated by the heat of fermentation (warm water) as drinking water for milking cows, and reduce the heating cost by using the hot water as a heat source for heating the floor of the delivery piggery. We are demonstrating the economic benefits of using heat.

従来、堆肥化装置における発酵熱の回収は、吸引通気式堆肥化装置において先行研究が行われてきた。吸引通気式堆肥化装置では堆肥資材が比較的高水分であり、通気速度も遅いため堆肥資材の粉塵が発生しにくい。また、粉塵が発生した場合は堆肥資材が堆積された堆肥発酵槽の底部の空気吸引穴で閉塞が発生する。このように、吸引通気式堆肥化装置では、排気中の粉塵含有率が低いため、排気通路に設けられる熱交換器において粉塵による閉塞が発生することはほぼなかった。このため、吸引通気式堆肥化装置における排気の除塵対策は不要であった。一方、中小家畜を中心に広く普及し、比較的容易に発酵熱を回収可能な密閉縦型堆肥化装置では、密閉した装置内でふん尿を機械的に攪拌、強制通気するため粉塵が発生しやすい。排気中の粉塵含有率が高いと、排気通路に設けられる熱交換器において粉塵による閉塞が発生し、熱交換効率の低下や排気通路からの悪臭漏れを招来する。そこで、水洗式の除塵装置(例えば、特許文献1)や排気管への籠状フィルタの設置(例えば、特許文献2)が考案されている。 Conventionally, the recovery of fermentation heat in a composting apparatus has been previously studied in a suction-ventilated composting apparatus. In the suction-ventilation type composting device, the compost material has a relatively high moisture content and the ventilation speed is slow, so that dust of the compost material is unlikely to be generated. In addition, when dust is generated, the air suction hole at the bottom of the compost fermenter where the compost material is deposited is blocked. As described above, in the suction-ventilation type composting device, since the dust content in the exhaust is low, the heat exchanger provided in the exhaust passage is hardly blocked by the dust. Therefore, it is not necessary to take measures to remove dust from the exhaust gas in the suction-ventilation type composting device. On the other hand, in a closed vertical composting device that is widely used mainly for small and medium-sized livestock and can recover fermentation heat relatively easily, dust is likely to be generated because manure is mechanically agitated and forcibly aerated in the closed device. .. If the dust content in the exhaust is high, the heat exchanger provided in the exhaust passage will be blocked by the dust, resulting in a decrease in heat exchange efficiency and leakage of a foul odor from the exhaust passage. Therefore, a water-washing type dust remover (for example, Patent Document 1) and installation of a cage-shaped filter on an exhaust pipe (for example, Patent Document 2) have been devised.

特開平11−128666号公報Japanese Unexamined Patent Publication No. 11-128666 特開2005―126308号公報Japanese Unexamined Patent Publication No. 2005-126308

しかしながら、水洗式の除塵装置はふん尿処理施設の付帯物としては高額であり、定期メンテナンスが必要となることからコスト面及び管理面の負担が大きい。また、排気管への籠状フィルタの設置は安価であるが、フィルタ部で粉塵による閉塞が発生するので頻繁なメンテナンスが必要になり、管理面の負担が大きい。フィルタ部の閉塞はスプレー洗浄装置等により除塵することで防止できるが、高コスト化が問題になる。このように従来の除塵対策はコスト面や管理面の負担が大きく、広く普及するに至っていない。 However, the flush type dust remover is expensive as an accessory of the manure treatment facility and requires regular maintenance, which imposes a heavy burden on cost and management. In addition, although it is inexpensive to install a cage-shaped filter in the exhaust pipe, frequent maintenance is required because the filter portion is blocked by dust, which imposes a heavy burden on management. Blockage of the filter portion can be prevented by removing dust with a spray cleaning device or the like, but there is a problem of high cost. As described above, the conventional dust removal measures have a large cost and management burden, and have not been widely used.

本発明は、上記事情に鑑みなされたもので、導入・管理負担を低減する除塵システム及び除塵方法の提供を目的とする。 The present invention has been made in view of the above circumstances, and an object of the present invention is to provide a dust removal system and a dust removal method that reduce the burden of introduction and management.

本発明に係る除塵システムは、密閉された堆肥発酵槽の上部から投入される堆肥原料を機械的に撹拌しつつ下部から強制通気して堆肥化処理を行う密閉縦型堆肥発酵槽と、前記密閉縦型堆肥発酵槽において発生する高熱源の気体を鉛直方向下方から鉛直方向上方に向けて誘導する排気通路と、前記排気通路の途中に配設され、前記気体の潜熱を熱利用する過程において生ずる結露水が滴下するように配置されたプレートフィンを介して低熱源体との熱交換を行う熱交換器と、を備え、前記気体が前記プレートフィンに対し鉛直方向下方から鉛直方向上方へと通過するときに熱交換が行われ、かつ、当該プレートフィンの下方に付着する前記気体に含まれていた塵を当該プレートフィンにおいて生じた結露水が当該プレートフィンの表面を滴下することで除去する、ことを特徴とする。 Dust system according to the present invention, a closed vertical composting fermentation tank which performs composting process with forced aeration from the bottom of the compost material to be introduced from the top of the closed compost fermentation tank while mechanically stirred, the sealing An exhaust passage that guides the gas of the high heat source generated in the vertical compost fermenter from the lower part in the vertical direction to the upper part in the vertical direction, and an exhaust passage that is arranged in the middle of the exhaust passage and is generated in the process of utilizing the latent heat of the gas. A heat exchanger for exchanging heat with a low heat source body via plate fins arranged so that condensed water drips is provided, and the gas passes from the lower part in the vertical direction to the upper part in the vertical direction with respect to the plate fins. heat exchange is performed when, and dew condensation water generated dust contained in the gas to adhere to the lower of the plate fins in the plate fins are removed by the dropwise addition of the surface of the plate fins, It is characterized by that.

本発明に係る除塵方法は、密閉された堆肥発酵槽の上部から投入される堆肥原料を機械的に撹拌しつつ下部から強制通気して堆肥化処理を行う密閉縦型堆肥発酵において発生する高熱源の気体を鉛直方向下方から鉛直方向上方に向けて誘導し、前記高熱源の気体の誘導経路の途中に配設され、当該高熱源の気体の潜熱を熱利用する過程において生ずる結露水が滴下するように配置されたプレートフィンを介して低熱源体との熱交換を行う熱交換器において、前記高熱源の気体が前記プレートフィンに対し鉛直方向下方から鉛直方向上方へと通過するときに熱交換が行われ、かつ、当該プレートフィンの下方に付着する前記高熱源の気体に含まれていた塵を当該プレートフィンにおいて生じた結露水が当該プレートフィンの表面を滴下することで除去する、ことを特徴とする。 Dust removal method according to the present invention occurs in a closed vertical composting fermenter of forced ventilation to composting process from the bottom of the compost material to be introduced from the top of the closed compost fermentation tank while mechanically stirred high The gas of the heat source is guided from the lower part in the vertical direction to the upper part in the vertical direction, and is arranged in the middle of the induction path of the gas of the high heat source, and condensed water generated in the process of utilizing the latent heat of the gas of the high heat source drops. In a heat exchanger that exchanges heat with a low heat source body through plate fins arranged so as to perform heat when the gas of the high heat source passes from the lower side in the vertical direction to the upper side in the vertical direction with respect to the plate fins. exchange is performed, and is removed by condensation water dust contained in the gas of the high heat source to adhere to the lower of the plate fins produced in the plate fins dripping the surface of the plate fin, it It is characterized by.

本発明によれば、上記課題を解決し、従来の負担を低減する除塵を行うことが可能となる。 According to the present invention, it is possible to solve the above problems and perform dust removal to reduce the conventional burden.

本発明の実施形態の除塵システムを示すブロック構成図である。It is a block block diagram which shows the dust removal system of embodiment of this invention. 本発明の実施形態の除塵システムにおける除塵作用を説明する図である。It is a figure explaining the dust removal action in the dust removal system of embodiment of this invention.

以下、本発明の実施形態について図面を参照して説明する。 Hereinafter, embodiments of the present invention will be described with reference to the drawings.

図1は本発明の実施形態の除塵システム100を示すブロック構成図である。本発明の実施形態の除塵システム100は、堆肥発酵槽10と、排気通路20と、第一熱交換器30と、第二熱交換器35と、第一排出口40と、第二排出口45とを有する施設において堆肥発酵熱の回収及び熱利用を行う工程に設けられる。なお、本発明の除塵システム100は、堆肥原料Tの堆肥化工程において発生する排気Hを外気で希釈せずに直接回収可能な密閉型の堆肥化施設への適用が好ましいが、例えばロータリー式やスクリュー式など自動式の堆肥化装置や堆積した堆肥をカーテンなどで覆い、堆肥上部の温暖で湿潤な空気を回収する施設であれば適用可能である。ここでは、密閉縦型堆肥化施設を例に説明する。 FIG. 1 is a block configuration diagram showing a dust removal system 100 according to an embodiment of the present invention. The dust removal system 100 of the embodiment of the present invention includes a compost fermenter 10, an exhaust passage 20, a first heat exchanger 30, a second heat exchanger 35, a first discharge port 40, and a second discharge port 45. It is provided in the process of recovering the heat of compost fermentation and utilizing the heat in the facility having the above. The dust removal system 100 of the present invention is preferably applied to a closed-type composting facility in which the exhaust H generated in the composting process of the compost raw material T can be directly recovered without being diluted with the outside air. It is applicable to automatic composting equipment such as screw type and facilities that cover the accumulated compost with curtains and collect the warm and moist air above the compost. Here, a closed vertical composting facility will be described as an example.

堆肥発酵槽10は、密閉縦型堆肥化装置である。堆肥発酵槽10は、密閉された堆肥発酵槽10の上部から投入される堆肥原料Tを機械的に攪拌・強制通気して堆肥化処理を行う。そして、堆肥発酵槽10の下部から内部に送風される空気は堆肥化物を通って堆肥発酵槽10の上部から排気される。このとき排気される排気Hは、堆肥化工程において発生した発酵熱を含み、高温(50℃以上)、高湿度(約100%RH)である。 The compost fermenter 10 is a closed vertical composting device. The compost fermenter 10 mechanically stirs and forcibly agitates the compost raw material T input from the upper part of the closed compost fermenter 10 to perform composting treatment. Then, the air blown from the lower part of the compost fermenter 10 to the inside is exhausted from the upper part of the compost fermenter 10 through the compost. The exhaust H exhausted at this time includes fermentation heat generated in the composting step, and has a high temperature (50 ° C. or higher) and a high humidity (about 100% RH).

排気通路20は、堆肥発酵槽10の上部から鉛直方向下方に排気Hを一旦誘導し、その後折り返して鉛直方向上方に向かうように配設された配管である。そして、排気通路20は、鉛直方向下方から鉛直方向上方に向かって排気Hが流れる排気通路20の途中に第一熱交換器30が配設される。本発明の除塵システム100は、排気Hが重力方向に逆行するように鉛直方向下方から鉛直方向上方に向かって流れる除塵通路部20aを排気通路20に設け、該除塵通路部20aに第一熱交換器30を設けることを特徴とする。本実施形態の排気通路20は、さらに、第一熱交換器30を通過した排気Hを鉛直方向上方から鉛直方向下方に向かって誘導するよう配管されており、除塵通路部20aの下流の通路上に第二熱交換器35が配設される。また、排気通路20には、第一熱交換器30の下方に第一排出口40と、第二熱交換器35の下方に第二排出口45とが設けられる。そして、第二熱交換器35を通過した排気Hは、排気通路20を通って排気Hの脱臭処理を行う脱臭装置へと誘導される。 The exhaust passage 20 is a pipe arranged so that the exhaust H is once guided downward in the vertical direction from the upper part of the compost fermenter 10 and then turned back and directed upward in the vertical direction. Then, in the exhaust passage 20, the first heat exchanger 30 is arranged in the middle of the exhaust passage 20 in which the exhaust H flows from the lower part in the vertical direction to the upper part in the vertical direction. In the dust removal system 100 of the present invention, the exhaust passage 20a is provided with a dust removal passage 20a that flows from the lower part in the vertical direction to the upper part in the vertical direction so that the exhaust H reverses in the direction of gravity, and the first heat exchange occurs in the dust removal passage 20a. It is characterized in that a vessel 30 is provided. The exhaust passage 20 of the present embodiment is further piped so as to guide the exhaust H that has passed through the first heat exchanger 30 from the upper part in the vertical direction to the lower part in the vertical direction, and is on the passage downstream of the dust removal passage portion 20a. A second heat exchanger 35 is arranged in the room. Further, the exhaust passage 20 is provided with a first exhaust port 40 below the first heat exchanger 30 and a second exhaust port 45 below the second heat exchanger 35. Then, the exhaust H that has passed through the second heat exchanger 35 is guided to a deodorizing device that deodorizes the exhaust H through the exhaust passage 20.

第一熱交換器30及び第二熱交換器35は、温度の異なる流体の間に配置された伝熱体を介して、該流体の熱交換を行う熱交換器であって、いわゆる、隔壁式熱交換器である。本実施形態に係る第一熱交換器30及び第二熱交換器35には、例えば、直交流プレーンフィン型熱交換器が用いられる。第一熱交換器30は、排気通路20の除塵通路部20aに設けられる。第一熱交換器30は、排気Hが鉛直方向下方から導入され、伝熱体であるプレートフィンを介して排気H(高熱源流体)と外気(低熱源流体)との間で、排気Hの発酵熱(潜熱)を熱利用するための熱交換が行われる。このとき、第一熱交換器30のプレートフィンには排気Hに含まれる粉塵Taが付着する。また、第一熱交換器30のプレートフィンには、排気Hより低温の外気との熱交換によって結露が発生する。本発明の除塵システム100は、第一熱交換器30のプレートフィンを、熱交換で生じる結露水Haによってプレートフィンに付着した粉塵Taを取り除く作用がある除塵フィルタとして機能させることを特徴とする。第一熱交換器30を介して加温された外気は、堆肥発酵槽10に入気される。第二熱交換器35は、除塵通路部20aの下流の排気通路20に設けられる。第二熱交換器35は、排気Hが鉛直方向上方から導入され、プレートフィンを介して排気H(高熱源流体)と水(低熱源流体)との熱交換が行われる。このときの排気Hには粉塵Taはほとんど含まれておらず、第二熱交換器35のプレートフィンにおける粉塵Taによる閉塞は生じない。除塵効果を有するのは、主として除塵通路部20aに設けられる第一熱交換器30である。第二熱交換器35を介して加温された水(温水)は家畜の飲用水や豚舎の床暖房の熱源として提供される。 The first heat exchanger 30 and the second heat exchanger 35 are heat exchangers that exchange heat of the fluids via heat transfer bodies arranged between fluids having different temperatures, and are so-called partition type. It is a heat exchanger. For the first heat exchanger 30 and the second heat exchanger 35 according to the present embodiment, for example, a orthogonal flow plane fin type heat exchanger is used. The first heat exchanger 30 is provided in the dust removal passage portion 20a of the exhaust passage 20. In the first heat exchanger 30, the exhaust H is introduced from below in the vertical direction, and the exhaust H is introduced between the exhaust H (high heat source fluid) and the outside air (low heat source fluid) via the plate fins which are heat transfer bodies. Heat exchange is performed to utilize the heat of fermentation (latent heat). At this time, dust Ta contained in the exhaust gas H adheres to the plate fins of the first heat exchanger 30. Further, dew condensation occurs on the plate fins of the first heat exchanger 30 due to heat exchange with the outside air having a temperature lower than that of the exhaust gas H. The dust removal system 100 of the present invention is characterized in that the plate fins of the first heat exchanger 30 function as a dust removal filter having an action of removing dust Ta adhering to the plate fins by the dew condensation water Ha generated by the heat exchange. The outside air heated via the first heat exchanger 30 is introduced into the compost fermenter 10. The second heat exchanger 35 is provided in the exhaust passage 20 downstream of the dust removal passage portion 20a. In the second heat exchanger 35, the exhaust H is introduced from above in the vertical direction, and heat exchange between the exhaust H (high heat source fluid) and water (low heat source fluid) is performed via the plate fins. The exhaust gas H at this time contains almost no dust Ta, and the plate fins of the second heat exchanger 35 are not blocked by the dust Ta. It is the first heat exchanger 30 provided mainly in the dust removing passage portion 20a that has the dust removing effect. The water (warm water) heated via the second heat exchanger 35 is provided as drinking water for livestock and as a heat source for floor heating of the piggery.

第一排出口40及び第二排出口45は、それぞれ第一熱交換器30及び第二熱交換器35で生じた結露水Ha(第一排出口40の場合は粉塵Taとともに)を排気通路20の外に排出するように各熱交換器の下方に位置する排気通路20の端部に配設され、排水トラップ構造によって封水する水蓋が設けられる。排水トラップ構造の封水部の水柱高さは、排気通路20の配管内圧力と大気圧とのバランスを考慮して、本実施形態の堆肥化装置の静圧と通気量であれば10センチ以上確保すれば十分である。なお、排気H中のアンモニアガス濃度が高く、結露水Ha中のアンモニア態窒素が硝酸性窒素濃度換算で放流基準濃度を超過する場合には、汚水処理施設や脱臭装置への誘導が必要になる。 The first discharge port 40 and the second discharge port 45 allow the dew condensation water Ha (in the case of the first discharge port 40, together with the dust Ta) generated in the first heat exchanger 30 and the second heat exchanger 35 to be exhausted through the exhaust passage 20. A water lid is provided at the end of the exhaust passage 20 located below each heat exchanger so as to discharge the water to the outside of the heat exchanger, and the water is sealed by the drain trap structure. The height of the water column of the water column of the water sealing part of the drain trap structure is 10 cm or more if the static pressure and the air volume of the composting device of the present embodiment are taken into consideration in consideration of the balance between the pressure inside the pipe of the exhaust passage 20 and the atmospheric pressure. It is enough to secure it. If the concentration of ammonia gas in the exhaust gas H is high and the ammonia nitrogen in the condensed water Ha exceeds the discharge standard concentration in terms of nitrate nitrogen concentration, it is necessary to guide it to a sewage treatment facility or a deodorizing device. ..

次に、図2は、本発明の除塵システムにおける除塵作用について説明する。具体的には、本発明の実施形態の排気通路20の除塵通路部20a、第一熱交換器30及び第一排出口40における除塵作用について詳細を説明する。 Next, FIG. 2 describes the dust removing action in the dust removing system of the present invention. Specifically, the dust removing action in the dust removing passage portion 20a, the first heat exchanger 30, and the first discharging port 40 of the exhaust passage 20 according to the embodiment of the present invention will be described in detail.

本実施形態の堆肥発酵槽10は密閉縦型堆肥化装置であり、装置内の上方空間には攪拌・通気によって発酵・乾燥した堆肥が粉塵Taとなって多く飛散している。よって、堆肥発酵槽10の上方から排気通路20に排気される排気Hには粉塵Taが多く含まれる。このため、排気Hが排気通路20の除塵通路部20aに設けられる第一熱交換器30を通過する際、排気中の粉塵Taが排気導入口側であるプレートフィン31の下方に多く付着する。ここで、第一熱交換器30の排気Hが通るプレートフィン31は、排気Hが除塵通路部20aと同様に鉛直方向下方から鉛直方向上方に向かって流れるよう設けられる。このため、熱交換によって排気Hが通過するプレートフィン表面に発生する結露の結露水Haが滴下し、粉塵Taを排気導入口側から下方に洗い流す。また、粉塵Taは、結露水Haと混ざって泥土化し、泥土自体の重力によって下方に落ちる。このように、第一熱交換器30のプレートフィン31が除塵フィルタとして機能し、プレートフィン31の排気導入口側から結露水Haによって粉塵Taを除去するとともに、重力方向に逆らって排気Hを第一熱交換器30に導入することで重力によって粉塵Taを排気から除去するので、第一熱交換器30の閉塞を防止する。また、プレートフィン31は、結露水Haによってクリーンな状態が維持されるので、除塵フィルタの機能低下、すなわち除塵効果の低下の招来を抑制することができる。そして、除去された粉塵Taや結露水Haは、除塵通路部20aを伝って第一排出口40から外部に排出される。 The compost fermenter 10 of the present embodiment is a closed vertical composting device, and a large amount of compost fermented and dried by stirring and aeration is scattered as dust Ta in the upper space inside the device. Therefore, the exhaust H exhausted from above the compost fermenter 10 to the exhaust passage 20 contains a large amount of dust Ta. Therefore, when the exhaust H passes through the first heat exchanger 30 provided in the dust removal passage portion 20a of the exhaust passage 20, a large amount of dust Ta in the exhaust adheres below the plate fin 31 on the exhaust introduction port side. Here, the plate fins 31 through which the exhaust H of the first heat exchanger 30 passes are provided so that the exhaust H flows from the lower side in the vertical direction to the upper side in the vertical direction, similarly to the dust removal passage portion 20a. Therefore, the dew condensation water Ha of dew condensation generated on the surface of the plate fin through which the exhaust H passes due to heat exchange drops, and the dust Ta is washed downward from the exhaust introduction port side. Further, the dust Ta is mixed with the condensed water Ha and becomes mud, and falls downward due to the gravity of the mud itself. In this way, the plate fins 31 of the first heat exchanger 30 function as a dust removal filter, and the dust Ta is removed from the exhaust inlet side of the plate fins 31 by the dew condensation water Ha, and the exhaust H is removed against the direction of gravity. By introducing the heat exchanger 30 into the heat exchanger 30, dust Ta is removed from the exhaust by gravity, so that the first heat exchanger 30 is prevented from being blocked. Further, since the plate fin 31 is maintained in a clean state by the dew condensation water Ha, it is possible to suppress the deterioration of the function of the dust removal filter, that is, the deterioration of the dust removal effect. Then, the removed dust Ta and dew condensation water Ha are discharged to the outside from the first discharge port 40 through the dust removal passage portion 20a.

なお、堆肥発酵槽10が通常の発酵状態であれば排気Hの相対湿度は常に100%RH近い値となり、排気温度が少し下がる程度の熱損失でも、熱交換によって除塵には十分な量の結露水Haが常時発生する。第一熱交換器30における結露水Haの発生を確実にするために外気の導入にファンを設けてもよい。また、排気Hの発生源として堆肥発酵槽10を挙げたが、塵と潜熱を含む気体であって、熱交換で潜熱を熱利用する過程で結露水を生じる高熱源となる気体を発生させる発生源であれば本発明の除塵システムを適用可能である。 If the compost fermenter 10 is in a normal fermentation state, the relative humidity of the exhaust H is always close to 100% RH, and even if the heat loss is such that the exhaust temperature drops a little, a sufficient amount of dew condensation can be removed by heat exchange. Water Ha is constantly generated. A fan may be provided for introducing the outside air in order to ensure the generation of condensed water Ha in the first heat exchanger 30. Further, the compost fermenter 10 was mentioned as the source of the exhaust H, but it is a gas containing dust and latent heat, and is generated to generate a gas that is a high heat source that generates dew condensation water in the process of utilizing the latent heat in heat exchange. If it is a source, the dust removal system of the present invention can be applied.

また、第一熱交換器30として直交流プレーンフィン型熱交換器を挙げたが、これに限らない。除塵フィルタとして機能可能な構造の熱交換器であればよい。すなわち、排気H(高熱源流体)を鉛直方向下方から鉛直方向上方に向かって導入することで、熱交換によって発生する結露水Haを排気導入口側(高熱源流体導入側)から排出可能な熱交換器であれば適用可能である。 Further, the orthogonal flow plane fin type heat exchanger is mentioned as the first heat exchanger 30, but the present invention is not limited to this. Any heat exchanger having a structure capable of functioning as a dust removal filter may be used. That is, by introducing the exhaust H (high heat source fluid) from the lower part in the vertical direction to the upper part in the vertical direction, the dew condensation water Ha generated by the heat exchange can be discharged from the exhaust introduction port side (high heat source fluid introduction side). It is applicable if it is a switch.

(実施形態の効果)
本発明の実施形態の除塵システムによれば、堆肥化装置からの堆肥発酵熱を用いることにより、コスト面や管理面の負担を低減した除塵を提供することができる。具体的には、堆肥化工程において発生した発酵熱を排気として熱回収することで、発酵熱による入気空気の加温や温水取得といった熱利用が熱交換器を介して可能になる発酵熱回収・利用サイクルが確立されてきたが、排気中の粉塵が多いタイプの堆肥化装置では、熱交換器で発生する結露水と排気中の粉塵とが混ざって泥土化し、泥土が熱交換器を閉塞してしまう課題があった。これに対し、従来は除塵装置を別途設けて対策していたが、本発明は、発酵熱回収・熱利用サイクルを活用し、熱交換によって高温・高湿度の排気から結露水が発生することを利用したものである。本発明の除塵システムは、堆肥化装置(気体の発生源)からの排気(潜熱と塵を含む高熱源の気体)を鉛直方向下方から鉛直方向上方に向かって誘導する排気通路上に熱交換器を配置し、熱交換器のプレートフィン(伝熱体)を除塵フィルタとして利用することで除塵機能の効果を得ることができるので、別途除塵装置を設けたり、除塵するためにポンプ等の可動装置を設けたりする必要がない。このように、これまでの排気通路の配管と熱交換器のレイアウトを変更するだけで除塵効果を得ることができるので、安価かつメンテナンスの負担がかからない除塵システム及び除塵方法を提供することができる。
(Effect of embodiment)
According to the dust removal system of the embodiment of the present invention, it is possible to provide dust removal with reduced cost and management burden by using the heat of compost fermentation from the composting apparatus. Specifically, by recovering heat from fermentation generated in the composting process as exhaust heat, heat utilization such as heating of incoming air by heat of fermentation and acquisition of hot water becomes possible through a heat exchanger. -Although the utilization cycle has been established, in composting equipment of the type with a large amount of dust in the exhaust, the dew condensation water generated in the heat exchanger and the dust in the exhaust are mixed and turned into mud, and the mud blocks the heat exchanger. There was a problem to do. On the other hand, in the past, a dust remover was separately provided to take measures, but the present invention utilizes a fermentation heat recovery / heat utilization cycle to generate dew condensation water from high temperature and high humidity exhaust by heat exchange. I used it. The dust removal system of the present invention is a heat exchanger on an exhaust passage that guides exhaust from a composting device (gas generation source) (gas of a high heat source including latent heat and dust) from downward in the vertical direction to upward in the vertical direction. The effect of the dust removal function can be obtained by using the plate fins (heat transfer body) of the heat exchanger as a dust removal filter. There is no need to provide. As described above, since the dust removal effect can be obtained only by changing the layout of the existing exhaust passage piping and the heat exchanger, it is possible to provide an inexpensive dust removal system and a dust removal method that do not require maintenance.

また、従来の排気通路が鉛直方向上方から鉛直方向下方に向かって排気を誘導する通路と地面に対して水平方向に排気を誘導する通路とで主に構成され、該通路上に熱交換器を配置していたところ、本発明の発明者らは、熱交換器で発生する結露水に着眼し、結露水を用いてプレートフィンに付着した粉塵を除去する本発明の除塵システム及び除塵方法に至った。本発明の排気通路は、鉛直方向下方から鉛直方向上方に向かって排気を誘導する通路を有し、該通路上に内部のプレートフィンが鉛直方向下方から鉛直方向上方に排気を誘導するよう設けられた熱交換器を配置する。このようなレイアウトによって、熱交換で発生する結露水によって熱交換器のプレートフィンが上から下へ常時洗浄され、結露水によって泥土化した粉塵は重力により下方に落ちる。また、熱交換器の下方から排気を導入するので、除塵の際に粉塵が熱交換器の排気導入口側から除去される。このため、熱交換器に粉塵が到達する前に重力によって粉塵を排気から除去することが可能であるとともに、熱交換器が鉛直方向上方から鉛直方向下方に向かって排気を誘導する通路上に配置される場合に比較して結露水によって泥土化した粉塵がプレートフィン内部を通過する量(内部滞留時間)を大幅に減らすことができる。また、熱交換器の下方には排水トラップ構造の排出口が設けられているので、重力によって落ちた粉塵や泥土及び結露水を速やかに排気通路の外に排出することができる。したがって、プレートフィンへの粉塵の付着が抑制され、熱交換器の閉塞を防止することができる。 Further, the conventional exhaust passage is mainly composed of a passage that guides the exhaust from the upper side in the vertical direction to the lower side in the vertical direction and a passage that guides the exhaust in the horizontal direction with respect to the ground, and a heat exchanger is installed on the passage. After arranging them, the inventors of the present invention focused on the dew condensation water generated in the heat exchanger, and reached the dust removal system and the dust removal method of the present invention for removing the dust adhering to the plate fins using the dew condensation water. It was. The exhaust passage of the present invention has a passage for guiding exhaust from the lower part in the vertical direction to the upper part in the vertical direction, and an internal plate fin is provided on the passage so as to guide the exhaust from the lower part in the vertical direction to the upper part in the vertical direction. Place a heat exchanger. With such a layout, the plate fins of the heat exchanger are constantly washed from top to bottom by the dew condensation water generated by the heat exchange, and the dust that has become muddy by the dew condensation water falls downward due to gravity. Further, since the exhaust gas is introduced from below the heat exchanger, the dust is removed from the exhaust introduction port side of the heat exchanger at the time of dust removal. Therefore, it is possible to remove the dust from the exhaust by gravity before the dust reaches the heat exchanger, and the heat exchanger is placed on the passage that guides the exhaust from the upper vertical direction to the lower vertical direction. The amount of dust that has become muddy due to condensed water passing through the inside of the plate fin (internal residence time) can be significantly reduced as compared with the case where the dust is formed. Further, since a drain trap structure discharge port is provided below the heat exchanger, dust, mud, and condensed water that have fallen due to gravity can be quickly discharged to the outside of the exhaust passage. Therefore, the adhesion of dust to the plate fins is suppressed, and the heat exchanger can be prevented from being blocked.

また、本発明によれば、熱交換で排気自体から発生する結露水と重力によって効果的に除塵し、熱交換と除塵を同時に行うことができる。このため、本実施形態のような排気中の粉塵含有率が高い堆肥化装置を長期稼働させることによる熱交換器の閉塞を防止することができるとともに、発酵熱回収・熱利用サイクルの効率低減や不具合発生を防止することができる。 Further, according to the present invention, dew condensation water generated from the exhaust gas itself and gravity can effectively remove dust by heat exchange, and heat exchange and dust removal can be performed at the same time. Therefore, it is possible to prevent the heat exchanger from being blocked by operating the composting apparatus having a high dust content in the exhaust gas for a long period of time as in the present embodiment, and to reduce the efficiency of the fermentation heat recovery / heat utilization cycle. It is possible to prevent the occurrence of problems.

このように、堆肥発酵熱を用いた除塵は、堆肥が発酵状態であれば常時結露水が発生するので、安定的に熱交換とともに行うことができる。よって、利用推進を促進させることができる。 As described above, dust removal using the heat of compost fermentation can be stably performed together with heat exchange because dew condensation water is always generated when the compost is in a fermented state. Therefore, it is possible to promote the promotion of utilization.

なお、本発明は上述した実施形態に何ら限定されるものではなく、本発明の技術的範囲に属する限り種々の態様で実施し得ることはいうまでもない。 It goes without saying that the present invention is not limited to the above-described embodiment, and can be implemented in various aspects as long as it belongs to the technical scope of the present invention.

例えば、上述した実施形態では、家畜ふん尿等の畜産廃棄物の堆肥化処理を例に挙げたが、一般廃棄物処理や産業廃棄物にも適用することができる。例えば、大量に発生する生ごみ等を回転ドラムや横置き堆肥発酵槽による発酵処理や乾燥処理によって減容化するシステムの他、塵と潜熱が含まれる気体中の塵除去にも適用可能である。 For example, in the above-described embodiment, the composting treatment of livestock waste such as livestock manure has been given as an example, but it can also be applied to general waste treatment and industrial waste. For example, it can be applied to a system that reduces the volume of a large amount of kitchen waste by fermentation treatment or drying treatment using a rotating drum or a horizontal compost fermenter, as well as dust removal in a gas containing dust and latent heat. ..

100 除塵システム
10 堆肥発酵槽(気体の発生源)
20 排気通路
20a 除塵通路部(気体誘導手段)
30 第一熱交換器(熱交換手段、除去手段)
31 プレートフィン(伝熱体)
35 第二熱交換器
40 第一排出口
45 第二排出口
T 堆肥原料
Ta 粉塵
H 排気
Ha 結露水
100 Dust removal system 10 Compost fermenter (gas source)
20 Exhaust passage 20a Dust removal passage (gas guiding means)
30 First heat exchanger (heat exchange means, removal means)
31 Plate fin (heat transfer body)
35 Second heat exchanger 40 First discharge port 45 Second discharge port T Compost raw material Ta Dust H Exhaust Ha Condensation water

Claims (5)

密閉された堆肥発酵槽の上部から投入される堆肥原料を機械的に撹拌しつつ下部から強制通気して堆肥化処理を行う密閉縦型堆肥発酵槽と、
前記密閉縦型堆肥発酵槽において発生する高熱源の気体を鉛直方向下方から鉛直方向上方に向けて誘導する排気通路と、
前記排気通路の途中に配設され、前記気体の潜熱を熱利用する過程において生ずる結露水が滴下するように配置されたプレートフィンを介して低熱源体との熱交換を行う熱交換器と、
を備え、
前記気体が前記プレートフィンに対し鉛直方向下方から鉛直方向上方へと通過するときに熱交換が行われ、かつ、当該プレートフィンの下方に付着する前記気体に含まれていた塵を当該プレートフィンにおいて生じた結露水が当該プレートフィンの表面を滴下することで除去する、
ことを特徴とする除塵システム。
A closed vertical compost fermenter that performs composting treatment by forcibly agitating the compost raw material input from the upper part of the closed compost fermenter from the lower part while mechanically stirring it.
An exhaust passage that guides the gas of the high heat source generated in the closed vertical compost fermenter from the lower part in the vertical direction to the upper part in the vertical direction.
A heat exchanger disposed in the middle of the exhaust passage and exchanging heat with a low heat source body via plate fins arranged so that dew condensation water generated in the process of utilizing the latent heat of the gas drops.
With
Heat exchange is performed when the gas passes into the vertically upward from vertically downward relative to the plate fins, and the dust contained in the gas to adhere to the lower of the plate fins in the plate fin The generated dew condensation water is removed by dropping the surface of the plate fin.
A dust removal system characterized by that.
前記排気通路は、前記プレートフィンから滴下する前記結露水及び前記塵を排出する排出口を前記熱交換器の下方に備える、
請求項1に記載の除塵システム。
The exhaust passage is provided below the heat exchanger with an exhaust port for discharging the condensed water and dust dripping from the plate fins.
The dust removal system according to claim 1.
前記排出口は、プレートフィンの下方に付着した前記塵と前記結露水と混ざった泥土が自重によって下方に落ちる泥土を除去可能な位置に配設される、
請求項2に記載の除塵システム。
The discharge port is arranged at a position where the mud mixed with the dust adhering to the lower part of the plate fin and the condensed water can remove the mud that falls downward due to its own weight.
The dust removal system according to claim 2.
前記熱交換器よりも前記気体の誘導方向における下流側にあり、鉛直方向上方から鉛直方向下方に向けて誘導する排気通路の途中に配設される第二の熱交換器をさらに備え、
前記第二の熱交換器は、前記塵が除去された前記気体と低熱源体としての水との熱交換によって当該を加温する、
請求項1乃至3のいずれか一項に記載の除塵システム。
A second heat exchanger, which is located downstream of the heat exchanger in the induction direction of the gas and is arranged in the middle of the exhaust passage for inducing the gas from the upper side in the vertical direction to the lower side in the vertical direction, is further provided.
Said second heat exchanger to warm the water by heat exchange with water as the gas and the low heat source body, wherein the dust is removed,
The dust removal system according to any one of claims 1 to 3.
密閉された堆肥発酵槽の上部から投入される堆肥原料を機械的に撹拌しつつ下部から強制通気して堆肥化処理を行う密閉縦型堆肥発酵において発生する高熱源の気体を鉛直方向下方から鉛直方向上方に向けて誘導し、
前記高熱源の気体の誘導経路の途中に配設され、当該高熱源の気体の潜熱を熱利用する過程において生ずる結露水が滴下するように配置されたプレートフィンを介して低熱源体との熱交換を行う熱交換器において、
前記高熱源の気体が前記プレートフィンに対し鉛直方向下方から鉛直方向上方へと通過するときに熱交換が行われ、かつ、当該プレートフィンの下方に付着する前記高熱源の気体に含まれていた塵を当該プレートフィンにおいて生じた結露水が当該プレートフィンの表面を滴下することで除去する、
ことを特徴とする除塵方法。
An enclosed composting fermenter high heat source gas generated in a closed vertical composting fermenter compost material is charged from the top with forced aeration from the bottom while mechanically stirred performs composting process from vertically downward Guide upward in the vertical direction,
Heat with the low heat source body via plate fins arranged in the middle of the induction path of the gas of the high heat source and arranged so that dew condensation water generated in the process of utilizing the latent heat of the gas of the high heat source drips. In the heat exchanger to be replaced
Heat exchange was performed when the gas of the high heat source passed through the plate fins from the lower part in the vertical direction to the upper part in the vertical direction, and was contained in the gas of the high heat source adhering to the lower part of the plate fins. condensation dust was generated in the plate fins are removed by the dropwise addition of the surface of the plate fins,
A dust removal method characterized by that.
JP2017082293A 2017-04-18 2017-04-18 Dust removal system and dust removal method Active JP6890318B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2017082293A JP6890318B2 (en) 2017-04-18 2017-04-18 Dust removal system and dust removal method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2017082293A JP6890318B2 (en) 2017-04-18 2017-04-18 Dust removal system and dust removal method

Publications (2)

Publication Number Publication Date
JP2018176103A JP2018176103A (en) 2018-11-15
JP6890318B2 true JP6890318B2 (en) 2021-06-18

Family

ID=64280642

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2017082293A Active JP6890318B2 (en) 2017-04-18 2017-04-18 Dust removal system and dust removal method

Country Status (1)

Country Link
JP (1) JP6890318B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112557071B (en) * 2020-11-05 2022-11-15 太原理工大学 Aerodynamic dust generating device

Family Cites Families (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ATE49469T1 (en) * 1981-04-09 1990-01-15 Heat Exchanger Ind Inc METHOD OF MAKING A HEAT EXCHANGER AND HEAT EXCHANGER ACCORDING TO THIS METHOD.
JPS63270376A (en) * 1987-04-30 1988-11-08 荏原実業株式会社 Composting and deodorization promoting device
JP3912871B2 (en) * 1997-10-30 2007-05-09 独立行政法人農業・食品産業技術総合研究機構 Deodorization equipment for livestock manure composting for cold regions
JP2001106587A (en) * 1999-10-06 2001-04-17 Kyowakiden Industry Co Ltd Organic composting equipment
JP2005126308A (en) * 2003-10-24 2005-05-19 Shizuoka Nichiden:Kk Apparatus for removing moisture in exhaust gas and dust in organic waste treatment device
CN107008138A (en) * 2017-04-14 2017-08-04 杭州瑞赛可环境工程有限公司 For the odor removal of rubbish aerobic fermentation equipment tail gas

Also Published As

Publication number Publication date
JP2018176103A (en) 2018-11-15

Similar Documents

Publication Publication Date Title
KR102284334B1 (en) Heat exchanger for food waste disposal
KR100976144B1 (en) Livestock excretions processing unit and livestock excretions processing
JP6890318B2 (en) Dust removal system and dust removal method
KR101017454B1 (en) Wet waste carbonization unit
CN107253791B (en) Dirt separating and drying device for intelligent environment-friendly toilet
KR20120060502A (en) Fermentation And Drying Device For Edible Waste Material
CN103224300B (en) Oil separator
JP2015132463A (en) Heat exchanger effluent collector
KR970014851A (en) Dry Fermentation Method of Food Waste and Its Dry Fermentation Apparatus
KR101258135B1 (en) Organic waste disposal apparatus using organic fermentating carrier
KR101580679B1 (en) Waste heat recovery unit for sludge dryer
CN209286999U (en) A kind of organic exhaust gas dehumidification equipment
CN104446727B (en) Organic material fermentation recovery processing equipment and processing method thereof
KR20100107990A (en) Appretus for treating organic wastes
CN216550196U (en) Production device for fertilizer and/or feed
JP2703513B2 (en) Organic substance high-speed decomposition drying equipment
JP2007319725A (en) Methane fermentation plant
CN208200706U (en) A kind of sludge deodorization system
KR101217891B1 (en) Device of food refuse disposal
KR100816488B1 (en) Manure Condensation Dryer
CN206566722U (en) A kind of cesspool foul gas collection and purification device
KR100525260B1 (en) Apparatus for disposal of sludge
CN223668951U (en) A gas dehydration device with improved dehydration effect
CN212327827U (en) Tail gas deodorization system
CN216038725U (en) Box processor for industrial waste liquid

Legal Events

Date Code Title Description
A80 Written request to apply exceptions to lack of novelty of invention

Free format text: JAPANESE INTERMEDIATE CODE: A80

Effective date: 20170427

A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20191204

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20200728

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20201006

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20201204

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20210209

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20210324

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20210511

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20210518

R150 Certificate of patent or registration of utility model

Ref document number: 6890318

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250