JP7457293B2 - Water remover - Google Patents
Water remover Download PDFInfo
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- JP7457293B2 JP7457293B2 JP2019199356A JP2019199356A JP7457293B2 JP 7457293 B2 JP7457293 B2 JP 7457293B2 JP 2019199356 A JP2019199356 A JP 2019199356A JP 2019199356 A JP2019199356 A JP 2019199356A JP 7457293 B2 JP7457293 B2 JP 7457293B2
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- water
- tank
- liquid
- oil
- hydrochloric acid
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 38
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 26
- 239000007788 liquid Substances 0.000 claims description 22
- 239000003921 oil Substances 0.000 claims description 19
- 229920003023 plastic Polymers 0.000 claims description 14
- 239000004033 plastic Substances 0.000 claims description 14
- 239000010812 mixed waste Substances 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 4
- 238000000197 pyrolysis Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 239000002906 medical waste Substances 0.000 claims description 3
- 239000000428 dust Substances 0.000 description 8
- 239000002699 waste material Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 229920000915 polyvinyl chloride Polymers 0.000 description 7
- 239000004800 polyvinyl chloride Substances 0.000 description 7
- 239000011550 stock solution Substances 0.000 description 4
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 3
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 229910052801 chlorine Inorganic materials 0.000 description 3
- 239000000460 chlorine Substances 0.000 description 3
- 239000003305 oil spill Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 238000005979 thermal decomposition reaction Methods 0.000 description 2
- 238000010333 wet classification Methods 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000292 calcium oxide Substances 0.000 description 1
- 235000012255 calcium oxide Nutrition 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000000502 dialysis Methods 0.000 description 1
- 238000009429 electrical wiring Methods 0.000 description 1
- 238000001962 electrophoresis Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 235000019645 odor Nutrition 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Images
Classifications
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- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Electrostatic Separation (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
Description
塩化ビニール製の混在廃プラなどを選別せずに熱分解してできた油や水に塩酸が混入して回収油の再利用の妨げになっていた。Hydrochloric acid was mixed into the oil and water produced by pyrolysis of mixed waste polyvinyl chloride plastics without sorting, which hindered the reuse of the recovered oil.
現状では混在している塩ビは目視で選別除去した後に破砕し、小片となった廃プラを搬送する工程で圧縮空気を用いた精密識別分級によってさらに残った塩ビ小片を吹き飛ばして除去する。しかし3P類の廃プラの小片の陰に塩ビ小片が隠れていた場合などではこれを識別できず除去できない。 Currently, the mixed PVC is visually sorted and removed, then crushed, and during the process of transporting the small pieces of waste plastic, the remaining small pieces of PVC are further blown away and removed through precision classification using compressed air. However, if a small piece of PVC is hidden behind a small piece of 3P waste plastic, it cannot be identified and removed.
以上述べた方法は乾式であり、多量の処理をする場合には人手によって大別した後に破砕し、洗浄工程の後に流水に浸し、浮いた軽い廃プラと沈んだ廃プラを分けるなどの湿式分級を行う。分級の効率や精度の向上のために水に塩分を加えるなどの方法もとられる。The above methods are dry methods, and when processing large quantities, the waste plastics are roughly separated by hand, then crushed, and after the washing process, they are immersed in running water to separate the floating, light waste plastics from the sinking waste plastics, and other wet classification methods are used. Methods such as adding salt to the water are also used to improve the efficiency and accuracy of classification.
混在廃プラから塩化物を完全に除去することは難しい。湿式分級の沈殿物は再利用されず埋め立てか焼却処理されている。この混在廃プラをそのまま熱分解処理した場合には回収油に多くの塩素分が混じり、燃料としての再利用の妨げとなる。バーナーなどの燃料に塩素を多く含む燃料を使用すると設備や機器が腐食してしまう。また臭気を出し、排出基準を満たす排ガスに浄化するのは難しい。 It is difficult to completely remove chloride from mixed waste plastic. The precipitate from wet classification is not reused but instead is disposed of in landfills or incinerated. If this mixed waste plastic is subjected to thermal decomposition treatment as it is, a large amount of chlorine will be mixed in the recovered oil, which will hinder its reuse as fuel. If fuel containing a lot of chlorine is used in burners, etc., equipment and equipment will corrode. It also emits odors and is difficult to purify into exhaust gas that meets emission standards.
固体の状態で完全に選別するのは不可能である。選別も洗浄もすることなく残液の残る容器などもそのまま処理して再利用できる方法について考える。プラスチックの原料は原油を精製する段階でできたナフサをポリマーにしたものなので廃棄物を油化させてナフサに還元することは可能である。 It is impossible to completely separate them in the solid state. We are thinking about ways to process and reuse containers with residual liquid without having to sort or wash them. The raw material for plastic is a polymer made from naphtha produced during the refining of crude oil, so it is possible to turn waste into oil and reduce it to naphtha.
医療廃棄物を収容した容器を開封して選別することは不可能である。廃プラを選別も洗浄もせず熱分解によって液化させ、液中でエマルジョン化した油と水と酸を分離できれば再利用の道が開かれる。 It is impossible to open and sort containers containing medical waste. If waste plastic can be liquefied through thermal decomposition without any sorting or cleaning, and the oil, water, and acid emulsified in the liquid can be separated, the path to reuse will be opened.
各家庭より出される一般廃プラは各種色々の種類が混入していて、塩化物の食品容器、湯バケツ、桶などの塩ビ製品や工業廃プラ耐酸製品などの塩ビ混入品、医療廃棄物中の透析チューブなど身近な塩化物を熱分解すると油の中や水の中に塩酸が混入し再利用の妨げとなっていた。 General waste plastics generated by households are mixed with various types, including chloride-containing PVC products such as food containers, hot water buckets, and buckets, PVC-containing products such as industrial waste plastic acid-resistant products, and medical waste. When chloride, which is commonly found in dialysis tubes, is thermally decomposed, hydrochloric acid gets mixed into the oil and water, hindering reuse.
油中に混入する塩酸の問題以外にも油の中に粉塵が混入するのも問題である。粉塵は熱分解槽温度300℃~350℃のときに多量に発生する。粉塵は発生ガスとともに熱分解槽外へ持ち出されて冷却液化する油や水に混入する。また粉塵は装置の内壁に付着して時間とともに硬化し、除塵に時間と手間がかかっていた。 In addition to the problem of hydrochloric acid mixed into oil, there is also the problem of dust mixed into oil. A large amount of dust is generated when the temperature of the pyrolysis tank is 300°C to 350°C. The dust is carried out of the pyrolysis tank along with the generated gas and mixed in with the oil and water that are cooled and liquefied. In addition, the dust adhered to the inner walls of the device and hardened over time, making dust removal time-consuming and labor-intensive.
発生した粉塵は高温の油や酸や水と混じり、強い粘性を持ち装置内部のあらゆるものに付着してプラントの機能を阻害する。この粉塵の発生を抑止する手段はない。 The generated dust mixes with hot oil, acid, and water, has a strong viscosity, and adheres to everything inside the equipment, hindering plant functionality. There is no way to prevent the generation of this dust.
除塵後のろ液混入後に清水を加水し、攪拌して加熱する。この液体を横長の形状の容器の一端より流入させてもう一端の上面に溢液する油を取り出す。またこの下方より水を抜き出す。塩酸は、槽底部のノックアウト槽に集合させる。 After mixing the filtrate after dust removal, clean water is added, stirred and heated. This liquid is allowed to flow into the horizontally long container from one end, and the oil overflowing onto the top surface of the other end is taken out. Also, drain the water from below. Hydrochloric acid is collected in a knockout tank at the bottom of the tank.
この横長形状の槽の液面に電極を浸す。電極は陽極と陰極を1組としてこれを多数組並べる。またこれら電極への電気配線や結線を行うための箱を槽の上に設置する。槽の断面形状は円形であり横に長い円筒形状である。電極は板形状でこの槽の左右中央部に位置する。電極の左右は流速を制限し、液体の槽での滞留時間を平均化するための邪魔板が設けられる。また邪魔板によって槽内での液体が分散されるため電極からの放電による液体分子の電気泳動の効率があがる。 The electrode is immersed in the liquid level of this oblong tank. Many sets of electrodes are arranged, each consisting of an anode and a cathode. Also, a box for electrical wiring and connection to these electrodes is installed on top of the tank. The tank has a circular cross-sectional shape and a horizontally long cylindrical shape. The electrodes are plate-shaped and located at the center of the left and right sides of this tank. Baffles are provided on the left and right sides of the electrode to limit the flow rate and equalize the residence time of the liquid in the tank. Further, since the liquid in the tank is dispersed by the baffle plate, the efficiency of electrophoresis of liquid molecules due to discharge from the electrodes is increased.
使用電源は200Vでも100Vでもよいが単相100Vであれば消費電力も少なく効率も充分であり経済的である。この電源を用いて電圧を1000V以上に昇圧し、乳化して液体中を浮遊する水の粒子に荷電する。荷電した水の粒子は電極の陽極に集まり、結合して液体中で自沈する。 The power source used may be 200V or 100V, but single-phase 100V is economical as it consumes less power and has sufficient efficiency. Using this power source, the voltage is increased to 1000 V or more, and water particles that are emulsified and suspended in the liquid are charged. The charged water particles collect at the anode of the electrode, combine and scuttle into the liquid.
油と水の中に塩酸が混入している。これは塩素を含む水分と油が乳化して親和してしまったために分離が難しくなったためである。この油と水の混合液に荷電することによって水の粒子のみを集合、結合させて液体中に沈め、比重分離することが可能となる。Hydrochloric acid is mixed into the oil and water. This is because the water containing chlorine emulsifies and the oil becomes more and more compatible, making it difficult to separate. By charging this oil and water mixture, only the water particles gather and bind together, sinking them into the liquid, making it possible to separate them by gravity.
〔図1〕は、本発明の除水機を側面より見た縦断面図である。槽の端面の蓋より2.原液流入管を槽内に向けて挿入する。管の槽内部分には多数の孔を設けることで流入液を槽内に分散させて流入させることができる。[Figure 1] is a vertical cross-sectional view of the water remover of the present invention seen from the side. 2. Insert the raw liquid inlet pipe into the tank from the cover on the end of the tank. By providing multiple holes in the tank part of the pipe, the inlet liquid can be dispersed and introduced into the tank.
流入原液は、槽内を3.油溢液管の方向に向けて流れるが槽内を移動する間は電極群に触れて反応して水分は下へ沈み、油水の境界がはっきりしてくる。流入した液体は槽内で油水に分離して油は3.油溢液管から、水は8.水排出口から排液される。槽の中央の底部には4.ノックアウトがあり、ここに塩酸が溜まる。ノックアウト下には7.排塩バルブがあり任意の周期でこれを開けることで塩酸を槽から排出する。 The inflow stock solution passes through the tank through 3. The water flows in the direction of the oil overflow pipe, but as it moves through the tank, it touches the electrodes and reacts, causing the water to sink to the bottom, and the boundary between the oil and water becomes clear. The inflowing liquid is separated into oil and water in the tank, and the oil is separated into 3. From the oil spill pipe, the water is 8. The liquid is drained from the water outlet. 4. At the bottom of the center of the tank. There is a knockout, and hydrochloric acid accumulates here. 7 below the knockout. There is a salt drain valve that can be opened at any time to drain hydrochloric acid from the tank.
槽内上部には6.電極群がある。電極の素材は非磁性体であり、陰極用と陽極用が交互に配置される。陰陽各1枚の電極板を1グループとしてこれらが多数並び、槽上の電極受けから吊り下げられる。 6. At the top of the tank. There is a group of electrodes. The material of the electrodes is non-magnetic, and the cathode and anode electrodes are alternately arranged. A large number of electrode plates, one each for yin and yang, are lined up and suspended from an electrode holder on the tank.
100Vを電源とし、これを10000~30000Vまで昇圧した電圧を電極群にかけ、槽内部の液体に微弱な電流を流す。液体の水分濃度、浸漬する電極の接液面積、電極間の距離によって流れる電流値は変わるが電源側に可変抵抗を設けることでで適正な電圧値と電流値に調整することができる。槽内の油溢液部付近に5.PH濃度センサーを設置してPH濃度を知ることができる。 Using 100V as a power source, a voltage boosted to 10,000 to 30,000V is applied to the electrode group, causing a weak current to flow through the liquid inside the tank. The current value that flows varies depending on the water concentration of the liquid, the contact area of the immersed electrodes, and the distance between the electrodes, but it can be adjusted to appropriate voltage and current values by providing a variable resistor on the power source side. 5. Near the oil spill part in the tank. You can know the PH concentration by installing a PH concentration sensor.
除水機は、原液が酸性のため材質はSUSか塩ビがよい。また原液は温度が高くなるため材料は厚みが厚いほうがよい。原液の塩酸濃度が20%を超えて高い場合には5%程度の生石灰水で中和処理してもよい。 The water remover should be made of SUS or PVC because the raw solution is acidic. Also, since the temperature of the stock solution becomes high, the material should be thicker. If the concentration of hydrochloric acid in the stock solution is higher than 20%, it may be neutralized with about 5% quicklime water.
混在廃プラスチックを選別しないで熱分解処理し、液化した後に塩酸を除去することができる。塩酸濃度0.05%以下にすることも可能である。 It is possible to thermally decompose mixed waste plastics without sorting them and remove hydrochloric acid after liquefying them. It is also possible to reduce the hydrochloric acid concentration to 0.05% or less.
1.横長槽
2.原液流入管
3.油溢液管
4.ノックアウト
5.PH濃度センサー
6.電極群
7.排酸バルブ
8.水排出口
9.邪魔板1.
Claims (2)
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2019199356A JP7457293B2 (en) | 2019-10-11 | 2019-10-11 | Water remover |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2019199356A JP7457293B2 (en) | 2019-10-11 | 2019-10-11 | Water remover |
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| Publication Number | Publication Date |
|---|---|
| JP2021062353A JP2021062353A (en) | 2021-04-22 |
| JP7457293B2 true JP7457293B2 (en) | 2024-03-28 |
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010031211A (en) | 2008-07-30 | 2010-02-12 | Ramusa Abe:Kk | Apparatus for desalting mixed waste plastic and concentrating hydrochloric acid |
| JP2011213962A (en) | 2010-04-02 | 2011-10-27 | San Life Kk | Method and apparatus for recovering decomposition oil of waste plastic |
| JP2016064404A (en) | 2014-07-30 | 2016-04-28 | 三菱マテリアル株式会社 | Oil-water separation device |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4804453A (en) * | 1982-06-07 | 1989-02-14 | National Tank Company | Resolution of emulsions with multiple electric fields |
| JP2867006B2 (en) * | 1993-07-08 | 1999-03-08 | トヨタ自動車株式会社 | Coagulation separation method and apparatus therefor |
| JP3627085B2 (en) * | 1997-03-31 | 2005-03-09 | 日立造船株式会社 | Waste plastic oil making equipment |
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- 2019-10-11 JP JP2019199356A patent/JP7457293B2/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2010031211A (en) | 2008-07-30 | 2010-02-12 | Ramusa Abe:Kk | Apparatus for desalting mixed waste plastic and concentrating hydrochloric acid |
| JP2011213962A (en) | 2010-04-02 | 2011-10-27 | San Life Kk | Method and apparatus for recovering decomposition oil of waste plastic |
| JP2016064404A (en) | 2014-07-30 | 2016-04-28 | 三菱マテリアル株式会社 | Oil-water separation device |
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