TW201005229A - Processing method for exhaust gas treatment device - Google Patents

Processing method for exhaust gas treatment device Download PDF

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Publication number
TW201005229A
TW201005229A TW97128931A TW97128931A TW201005229A TW 201005229 A TW201005229 A TW 201005229A TW 97128931 A TW97128931 A TW 97128931A TW 97128931 A TW97128931 A TW 97128931A TW 201005229 A TW201005229 A TW 201005229A
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Taiwan
Prior art keywords
oil
gas
furnace
cracking
exhaust gas
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TW97128931A
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Chinese (zh)
Inventor
Qing-Kun Zhuang
Wei-Jia Wu
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Qing-Kun Zhuang
Wei-Jia Wu
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Application filed by Qing-Kun Zhuang, Wei-Jia Wu filed Critical Qing-Kun Zhuang
Priority to TW97128931A priority Critical patent/TW201005229A/en
Publication of TW201005229A publication Critical patent/TW201005229A/en

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  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

The invention provides a processing method for exhaust gas treatment device. Plastic disposal related to petrochemical products (e.g. polypropylene, polyethylene and polycarbonate) is burned through the inside of the feeding furnace and is cracked through the pyrolysis furnace at 250-400 degrees Celsius of pyrolysis temperature so that related products such as plastic disposals are burned and gasified. Further, an auxiliary material is placed into the stirring device from the furnace opening and is cooled and condensed with the plastic exhaust gas after stirring. Water, gas and oil are then separated by the oily water separator and the oil gas separator. The oil can be introduced into the oil storage tank to completely evaporate residual water content via a distiller at about 250 degrees Celsius so that oil gas therein can be cooled and condensed, and the solvent, gasoline and diesel fuel, and fuel oil can be separated, wherein the combustible oil gas can flow back to the pyrolysis furnace again to be combusted again.

Description

201005229 八、發明說明: 【發明所屬之技術領域】 本發明是提供一種廢氣處理裝置的處理方法,主要 是對石化相關產品(如聚丙嫦(Polyproylene, PP)、聚乙 稀(Polyethylene, PE)、聚碳酸酯樹脂(polycarbonate, PC)) 的塑膠廢棄物可透過一廢氣處理裝置予以高溫燃燒裂 解,及將其間的水、油氣、瓦斯予以分離出,並使區分 、出的可燃燒油氣再度回流至鍋爐作再次燃燒使用的具 環保防空污設計。 【先前技術】 按,目前對生活周遭所使用的石化相關產品,如聚 丙烯(Polyproylene,PP)、聚乙烯(Polyethylene, PE)、聚碳 酸酯樹脂(polycarbonate,PC)其塑躍廢棄物在經回收後 通常是加以高溫以重新製成再生原料,作為適合性質的 產品製造;但對一些須作複雜的清理才可成為再生原料 )提煉的塑膠廢棄物,業者通常是直接以高溫燃燒予以銷 毀,以致造成破壞環境的空氣污染。 【發明内容】 本發明即是依既有作為處理石化相關產品其塑膠 廢棄物的方法所存缺失來作一可具體克服空污的處理 方法,以期該石化相關產品(如聚丙婦(Polyproylene, PP)、聚乙婦(Polyethylene, PE)、聚破酸酯樹脂 (polycarbonate,PC))的塑膠廢棄物可透過一廢氣處理裝 201005229 置予以高溫燃燒裂解,及將其間的水、油氣、瓦斯予以 分離出,並使區分出的可燃燒油氣再度回流至鍋爐作再 次燃燒使用的具環保防空污設計。 本發明之主要目的,是將石化相關產品(如聚丙烯 (Polyproylene,PP)、聚乙烯(Polyethylene,PE)、聚破酸酯 樹脂(polycarbonate,PC))的塑膠廢棄物經由進料爐口内 部燃燒並以裂解溫度250°C〜400°C的裂解爐予以裂 解,使塑膠廢棄物等相關產品予以燃燒氣化;及在攪拌 裝置其爐口置入以輔助物料來與塑膠廢氣在攪拌裝置 内予以攪拌;使該結合有塑膠廢氣的物料予以冷卻凝 縮;再經一油水分離器予以分離出水並外排出;繼經一 ^ 油氣分離器予以分離出瓦斯及油,該瓦斯則引至裂解爐 内,該油則引至儲油槽内;對引入儲油槽其間的油可經 一蒸餾器以大約250°C的溫度將殘留的水氣予以完全蒸 發,在使其間的油氣予以冷卻凝縮,並區分出溶劑類、 )汽柴油、举料油之類;在使該區分出並儲存其間的可燃 燒油氣再度予以回流至裂解爐作再次的燃燒使用。 本發明之第二目的,是對經由進料爐口其内部以裂 解温度250°C〜400°C的裂解爐予以燃燒裂解後的塑膠 廢棄物渣是可作為辅助原料以供再生使用的燃燒。 【實施方式】 本發明設計的廢氣處理裝置的處理方法,參第一、 二圖,其實施步驟是包含以: 201005229 a··將石化相關產品(如聚丙婦(poiyproyiene,PP)、 聚乙烯(Polyethylene,PE)、聚碳酸酯樹脂(polycarb〇nate, PC))的塑膠廢棄物經由進料爐口(丨丨)内部燃燒並以裂解 溫度250°C〜40(TC的裂解爐(1)予以裂解,使塑膠廢棄 物等相關產品予以燃燒氣化,其中對燃燒後的塑膠廢棄 物渣(如附件一)是可作為輔助原料以供再生使用的燃 燒; ·’、 b·在攪拌裝置(2)其爐口置入以輔助物料來與塑膠 廢氣在授掉裝置(2)内予以攪拌; c. 使該結合有塑膠廢氣的物料在冷卻裝置内予 以冷卻凝縮; d. 再經一油水分離器(4)予以分離出水並外排出; e·繼經-油氣分離器⑸予以分離出瓦 兮 瓦斯則引至裂解爐⑴内,該油則5_油槽⑻由内該 # f·對引入儲油槽⑹其間的油(如附件 ,一201005229 VIII. Description of the Invention: [Technical Field] The present invention provides a treatment method for an exhaust gas treatment device, mainly for petrochemical related products (such as Polyproylene (PP), Polyethylene (PE), Polycarbonate (PC) plastic waste can be burned and cracked at high temperature through an exhaust gas treatment device, and the water, oil and gas and gas between them are separated, and the differentiated and combustible oil and gas are returned to the same. The boiler is designed to be re-burned with an environmentally friendly air pollution prevention design. [Prior Art] According to the petrochemical-related products used in daily life, such as polypropylene (Polyproylene, PP), polyethylene (Polyethylene, PE), polycarbonate resin (polycarbonate, PC) After recycling, it is usually reheated to a high temperature to be reconstituted as a product of suitable properties; but for some plastic wastes that need to be cleaned up to become a recycled raw material, the manufacturer usually destroys it directly at high temperature. This causes air pollution that damages the environment. SUMMARY OF THE INVENTION The present invention is a treatment method that can specifically overcome air pollution according to the existing method for treating plastic wastes related to petrochemical related products, with a view to the petrochemical related products (such as Polyproylene (PP)). The plastic waste of Polyethylene (PE) and polycarbonate (PC) can be pyrolyzed and cracked through an exhaust gas treatment equipment 201005229, and the water, oil and gas and gas are separated therefrom. And the differentiated combustible oil and gas is returned to the boiler for re-combustion with an environmentally-friendly air pollution design. The main purpose of the present invention is to pass plastic wastes of petrochemical related products (such as polypropylene (PP), polyethylene (PE), polycarbonate (PC)) through the inlet of the feed furnace. It is burned and cracked in a cracking furnace with a cracking temperature of 250 ° C to 400 ° C to burn and vaporize related products such as plastic waste; and the auxiliary device is placed in the stirring port of the stirring device to assist the material and the plastic waste gas in the stirring device. Stirring; the material combined with the plastic waste gas is cooled and condensed; and then separated by a water separator to discharge water and discharged; after a gas separator is separated, gas and oil are separated, and the gas is introduced into the cracking furnace. The oil is introduced into the oil storage tank; the oil introduced into the oil storage tank can completely evaporate the residual water gas through a distiller at a temperature of about 250 ° C, and the oil and gas between them is cooled and condensed, and the oil is separated and distinguished. Solvents, ) gasoline and diesel, cooking oil, and the like; the combustible oil and gas that is separated and stored therebetween is again returned to the cracking furnace for re-combustion. A second object of the present invention is to burn a plastic waste slag which has been burned and cracked in a cracking furnace having a cracking temperature of 250 ° C to 400 ° C through a feed furnace port, and is used as an auxiliary material for regeneration. [Embodiment] The treatment method of the exhaust gas treatment device designed by the present invention is referred to in the first and second figures, and the implementation steps thereof are included to: 201005229 a···Petrochemical related products (such as poiyproyiene (PP), polyethylene ( Polyethylene, PE), polycarbonate resin (polycarb〇nate, PC)) plastic waste is burned inside the feed furnace mouth (丨丨) and is cracked at a temperature of 250 ° C ~ 40 (TC cracking furnace (1) Cracking, the plastic waste and other related products are burned and vaporized, wherein the burned plastic waste slag (such as Annex 1) is a combustion that can be used as an auxiliary material for regeneration; · ', b · in the stirring device (2 The furnace mouth is placed with auxiliary material to stir the plastic waste gas in the transfer device (2); c. the material combined with the plastic waste gas is cooled and condensed in the cooling device; d. (4) Separate the water and discharge it; e. Follow the gas-oil separator (5) to separate the corrugated gas into the cracking furnace (1), the oil is 5_ oil tank (8) from the inside #f· pairs into the oil storage tank (6) Oil in between (if attached) Piece, one

条館器⑺以大祕代的温度將殘㈣水氣予H Μ:其::油氣予以冷卻凝縮,並區分出= m八柴油、燃料油之類; ⑷ =在使㈣分出並儲存其間的可燃燒油 回流至裂解爐⑴作再次的峨使用。、 201005229 【圖式簡單說明】 第一圖:本發明廢氣處理裝置的流程方塊圖 第二圖:本發明廢氣處理裝置的流程示意圖 附件一:本發明經燃燒後的塑膠廢棄物渣實物照片 附件二:本發明經油氣分離器予以分離的油實物照 片 附件三:本發明經台灣中油煉製研究所檢驗報告 【主要元件符號說明】 〔本發明〕 (11)爐口 (3)冷卻裝置 (5)油氣分離器 (7)蒸餾器 (1) 裂解爐 (2) 攪拌裝置 (4)油水分離器 (6)儲油槽The pavilion (7) will remnant (4) water vapor to H Μ at the temperature of the big secret: its:: oil and gas will be cooled and condensed, and distinguish between m 8 diesel, fuel oil and the like; (4) = when (4) is separated and stored The combustible oil is returned to the cracking furnace (1) for further use. , 201005229 [Simplified description of the drawings] The first diagram: the flow chart of the exhaust gas treatment device of the present invention, the second diagram: the flow diagram of the exhaust gas treatment device of the present invention. Annex I: Photograph of the physical waste slag of the present invention : Photograph of the actual oil of the oil separated by the oil and gas separator of the present invention. Attachment 3: The invention is inspected by the Taiwan National Petroleum Research Institute [Explanation of main component symbols] [Invention] (11) Furnace (3) cooling device (5) Oil and gas separator (7) distiller (1) cracking furnace (2) stirring device (4) oil water separator (6) oil storage tank

Claims (1)

201005229 九、申請專利範園: 1. 一種廢氣處理裝置的處理方法,其實施步驟包含 以: a. 將石化相關產品的塑膠廢棄物經由進料爐口内 部燃燒並以裂解溫度2 5 0 °C〜4 0 0 °C的裂解爐予以裂 解,使塑膠廢棄物等相關產品予以燃燒氣化; b. 在攪拌裝置其爐口置入以輔助物料來與塑膠廢 氣在攪拌裝置内予以攪拌; c. 使該結合有塑膠廢氣的物料在冷卻裝置内予以 冷卻凝縮; d. 再經一油水分離器予以分離出水並外排出; e. 繼經一油氣分離器予以分離出瓦斯及油,該瓦斯 則引至裂解爐内,該油則引至儲油槽内; f. 對引入儲油槽其間的油可經一蒸餾器以大約250 °C的溫度將殘留的水焉予以完全蒸發,在使其間的油氣 予以冷卻凝縮,並區分出溶劑類、汽柴油、燃料油之類; g. 在使該區分出並儲存其間的可燃燒油氣再度予 以回流至裂解爐作再次的燃燒使用。 2.如申請專利範圍第1項所述之廢氣處理裝置的處 理方法,其中該經由進料爐口其内部以裂解溫度250°C 〜400°C的裂解爐予以燃燒裂解的石化相關產品其塑膠 廢棄物是以聚丙稀(Polyproylene,PP)、聚乙烯 (Polyethylene,PE)、聚碳酸 S旨樹腊(polycarbonate, PC)為 201005229 實施。 3.如申請專利範圍第1項所述廢氣處理裝置的處理 方法,其中該經由進料爐口其内部以裂解溫度250°C〜 400°C的裂解爐予以燃燒裂解後的塑膠廢棄物渣是可作 為輔助原料以供再生使用的燃燒。201005229 IX. Application for Patent Park: 1. A method for treating an exhaust gas treatment device, the implementation steps of which include: a. burning the plastic waste of the petrochemical-related product through the inside of the feed furnace mouth and using a cracking temperature of 250 ° C The cracking furnace of ~400 °C is cracked to make the plastic waste and other related products burned and gasified; b. The auxiliary device is placed at the mouth of the stirring device to stir the plastic waste gas in the stirring device; c. The material combined with the plastic waste gas is cooled and condensed in the cooling device; d. the water is separated by an oil water separator and discharged; e. After separating the gas and the oil through an oil and gas separator, the gas is introduced In the cracking furnace, the oil is introduced into the oil storage tank; f. The oil introduced into the oil storage tank can be completely evaporated by a distiller at a temperature of about 250 ° C, and the oil and gas between them is given Cooling and condensing, and distinguishing between solvents, gasoline and diesel, fuel oil, etc.; g. re-compressing the combustible oil and gas that is separated and stored in the cracking furnace for re-combustion use. 2. The method for treating an exhaust gas treatment device according to claim 1, wherein the plasticization-related product is fire-decomposed by a cracking furnace having a cracking temperature of 250 ° C to 400 ° C inside the feed furnace port. The waste was implemented as Polyproylene (PP), Polyethylene (PE), and Polycarbonate (PC) 201005229. 3. The method for treating an exhaust gas treatment device according to claim 1, wherein the plastic waste residue after combustion and cracking is carried out through a cracking furnace having a cracking temperature of 250 ° C to 400 ° C inside the feed furnace port. It can be used as an auxiliary material for combustion for regeneration.
TW97128931A 2008-07-30 2008-07-30 Processing method for exhaust gas treatment device TW201005229A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI495835B (en) * 2011-03-16 2015-08-11

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI495835B (en) * 2011-03-16 2015-08-11

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