KR20060009635A - Oil reductor waste synthetic resin - Google Patents

Oil reductor waste synthetic resin Download PDF

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Publication number
KR20060009635A
KR20060009635A KR1020040058296A KR20040058296A KR20060009635A KR 20060009635 A KR20060009635 A KR 20060009635A KR 1020040058296 A KR1020040058296 A KR 1020040058296A KR 20040058296 A KR20040058296 A KR 20040058296A KR 20060009635 A KR20060009635 A KR 20060009635A
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South Korea
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oil
distillation
synthetic resin
chamber
waste synthetic
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KR1020040058296A
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Korean (ko)
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조위수
김기헌
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조위수
김기헌
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Priority to KR1020040058296A priority Critical patent/KR20060009635A/en
Publication of KR20060009635A publication Critical patent/KR20060009635A/en

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    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10—Feedstock materials
    • C10G2300/1003—Waste materials
    • 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
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00—Technologies for the production of fuel of non-fossil origin
    • Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
    • 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

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

본 발명은 폐합성수지로부터 오일을 얻도록 하는 오일환원장치에 관한 것으로, 용융기를 통한 페합성수지의 용융으로 발생된 기체유기증기가 증류관(2) 하부의 여과실(4)이 갖는 필터(10)를 통과하여 여과되고, 여과 후 연통관(8)과 차단판 (12) 사이에 갖는 틈을 통하여 증류실(6)에 유입되면 냉각기(13)에 의한 액체화로 낙하하여 증류실(6) 일측 하부에 갖는 오일배출관(14)으로 배출되도록 한 것으로서, 간단한 구조로 설치비용을 줄일 수 있고 또 기체유기증기의 원활한 흐름 및 액체화된 오일의 신속한 회수로 생산성향상을 가져올 수 있도록 한 것이다.The present invention relates to an oil reduction device for obtaining oil from a waste synthetic resin, wherein the gas organic vapor generated by melting of the synthetic resin through a melter is provided in the filter chamber (4) below the distillation tube (2). After filtration, the filtration is introduced into the distillation chamber 6 through the gap between the communication tube 8 and the blocking plate 12, and falls into the liquefaction by the cooler 13 to the lower portion of one side of the distillation chamber 6 As it is to be discharged to the oil discharge pipe 14 having, it is possible to reduce the installation cost with a simple structure and to improve productivity by the smooth flow of gas organic vapor and the rapid recovery of the liquid oil.

Description

폐합성수지의 오일환원장치{OIL REDUCTOR WASTE SYNTHETIC RESIN}Oil reduction device of waste synthetic resin {OIL REDUCTOR WASTE SYNTHETIC RESIN}

도 1 : 본 발명의 단면구성도.1 is a cross-sectional view of the present invention.

<도면의 주요부분에 대한 부호의 설명><Description of the symbols for the main parts of the drawings>

(2)--증류관 (4)--여과실(2)-distillation tube (4)-filter room

(6)--증류실 (8)--연통관(6)-distillation chamber (8)-communicator

(10)--필터 (12)--차단판(10)-filter (12)-blocking plate

(13)--냉각기 (14)--오일배출관(13)-Cooler (14)-Oil Discharge Tube

(16)--가스배출관 (18)--격판(16)-Gas exhaust pipe (18)-Plate

(20)--망판 (22)--글라스화이바(20)-Hazetone (22)-Glass Fiber

(24)--유통로(24)-Distribution Path

본 발명은 폐합성수지로부터 휘발유나 경유 등 오일을 회수하는 오일환원장치에 관한 것이다.The present invention relates to an oil reduction apparatus for recovering oil, such as gasoline or diesel, from a waste synthetic resin.

비닐이나 플라스틱 등 각종 폐합성수지로부터 오일을 회수하는 오일환원장치에 대하여는 특허출원 제2003-5317호를 제공한 바 있다.Patent Application No. 2003-5317 has been provided for an oil reduction apparatus for recovering oil from various waste synthetic resins such as vinyl or plastic.

상기 특허는 폐합성수지의 용융으로 발생된 기체유기증기가 다단계의 필터를 통과하면서 불순물이 제거되고, 불순물이 제거된 기체유기증기는 분해반응기를 통한 분자반응 및 촉매크래킹반응 후 냉각기를 통과하면서 냉각되어 액체화된 오일을 얻도록 구성된다.The patent discloses that the gas organic vapor generated by melting the waste synthetic resin passes through a multi-stage filter, and impurities are removed, and the gas organic vapor from which the impurities are removed is cooled while passing through a cooler after a molecular reaction and a catalytic cracking reaction through a decomposition reactor. And to obtain a liquefied oil.

따라서 다단계의 필터와 별도의 분해반응기 및 독립된 공간에 냉각기를 갖는 복잡한 구조로서, 설치비용 부담이 크고 또 부피가 커 공간활용률이 떨어지게 되며, 기체유기증기가 다단의 필터와 분해반응기 및 냉각기를 통과하여 액체화된 오일을 얻기까지 흐름이 원활하지 못할뿐 아니라 액체화된 오일은 냉각기의 통과로 회수되게 하므로서 생산성이 저하되는 등의 문제점들이 지적되고 있는 것이다.Therefore, as a complex structure having a multi-stage filter, a separate decomposition reactor, and a cooler in an independent space, the installation cost is large and the volume is large, and the space utilization rate is reduced. Not only the flow is not smooth until the liquid oil is obtained, but also the problems such as lowering the productivity by allowing the liquid oil to be recovered through the passage of the cooler has been pointed out.

본 발명은 상술한 종래기술이 갖는 문제점들을 해결하고자 간단한 구조로 설치비용부담을 줄일 수가 있고 또 부피가 작아 공간활용률을 높여줄 수가 있으며, 기체유기증기의 원활한 흐름 및 액체화된 오일의 신속한 회수로 생산성을 높여줄 수가 있는 오일환원장치를 제공하고자 한다.The present invention can reduce the installation cost burden with a simple structure in order to solve the problems of the prior art described above, and can increase the space utilization rate because of the small volume, the productivity by smooth flow of gas organic vapor and rapid recovery of the liquefied oil To provide an oil reduction device that can increase the.

상기한 목적달성을 위하여 본 발명은 용융기로부터 발생된 기체유기증기가 여과실의 필터를 통과하면서 여과되고, 여과된 기체유기증기는 연통관과 차단판사이에 갖는 틈을 통하여 증류실에 유입되면 냉각기에 의한 액체화로 낙하하여 증류실 일측 하부에 갖는 오일배출관을 통하여 회수되도록 구성함을 특징으로 한다.In order to achieve the above object, the present invention is a gas organic vapor generated from the melter is filtered while passing through the filter of the filter chamber, the filtered gas organic vapor is introduced into the distillation chamber through the gap between the communication tube and the blocking plate to the cooler Falling to the liquid by means of characterized in that configured to be recovered through the oil discharge pipe having a lower side of the distillation chamber.

도1은 본 발명의 단면구성도로서, 본 발명은 용융기 상부에 연장형성되는 증 류관(2)과, 상기 증류관(2) 중앙부에 형성되어 하부의 여과실(4)과 상부의 증류실(6)을 연통하는 연통관(8)과, 여과실(4)내에 갖는 필터(1)와, 연통관(8)상부에 갖는 차단판(12)과, 증류실(6) 내에 갖는 냉각기(13)와, 증류실의 일측 하부에 갖는 오일배출관(14) 및 증류실 상부에 갖는 가스배출관(6)으로 구성된다.1 is a cross-sectional configuration of the present invention, the present invention is a distillation pipe (2) extending in the upper part of the melter, and formed in the center of the distillation pipe (2) and the lower filtration chamber (4) and the upper distillation chamber The communication tube 8 communicating with (6), the filter (1) provided in the filtration chamber (4), the blocking plate (12) provided in the upper communication tube (8), and the cooler (13) provided in the distillation chamber (6). And an oil discharge pipe 14 provided at one lower portion of the distillation chamber and a gas discharge pipe 6 provided at an upper portion of the distillation chamber.

상기에 있어, 증류관(2)의 여과실(4)과 증류실(6) 사이에 갖는 연통관(8)은 격판(18)의 중앙부로부터 적정높이로 돌출형성되며, 그 상부에 갖는 차단판(12)은 연통관(8)에 비해 크고 또 단부로 갈수록 하향경사진 형태로서 연통관(8)과 적정간격을 두고 고정설치된다.In the above, the communication tube 8 provided between the filtration chamber 4 and the distillation chamber 6 of the distillation tube 2 protrudes from the central portion of the diaphragm 18 at an appropriate height, and has a blocking plate having an upper portion thereof ( 12) is larger than the communication tube (8) and is fixed to the communication tube (8) at an appropriate interval in the form of inclined downward toward the end.

또한 여과실(4) 내에 갖는 필터(10)는 스테인레스로된 상하망판(20) 사이에 직경 1∼3mm로서 길이 8∼13cm의 글라스화이바(22)가 약 8∼15cm 두께로 충진된 것으로서, 물이 약간의 지체 시간을 갖고 배출될 수 있는 정도의 밀도를 갖는 것이면 필터로서의 기능을 충분히 만족할 수 있는 것으로 확인하였다.In addition, the filter 10 included in the filtration chamber 4 is filled with a glass fiber 22 having a diameter of 1 to 3 mm and a length of 8 to 13 cm between the upper and lower half panels 20 made of stainless steel and having a thickness of about 8 to 15 cm. It was confirmed that the function as a filter can be sufficiently satisfied as long as it has this delay time and the density which can be discharged | emitted.

한편 증류실(6)에 형성되는 냉각기(13)는 수개의 유통로(24)를 갖는 것으로서, 냉각수 내지는 냉매의 순환으로 냉각이 이루어지도록 구성된다.On the other hand, the cooler 13 formed in the distillation chamber 6 has several flow passages 24, and is configured to cool by circulation of cooling water or refrigerant.

증류실(6)의 일측 하부에 갖는 오일배출관(14)은 격판(18)에 비해 낮게 형성되고, 증류실(6) 상부에 갖는 가스배출관(16)은 용융기를 가열하는 가스버너 등과 연결구성된다.The oil discharge pipe 14 having one lower portion of the distillation chamber 6 is lower than the diaphragm 18, and the gas discharge pipe 16 having the upper portion of the distillation chamber 6 is connected to a gas burner for heating the melter. .

본 발명은 용융기 상부에 연장형성되는 증류관(2)내에 연통관(8)을 갖는 격판(18)을 사이에 두고 필터(10)와 냉각기(13)를 갖도록 하고, 연통관(8) 상부에는 차단판(12)을 갖도록 하며, 증류실(6)은 오일배출관(14)과 가스배출관(16)을 갖도 록 하는 것으로 만족하므로 구조를 간단히할 수가 있고 또 그 부피를 최소화할 수가 있게 된다.The present invention includes a filter (10) and a cooler (13) with a diaphragm (18) having a communication tube (8) in the distillation tube (2) extending on the upper part of the melter, and cut off the upper communication tube (8) The plate 12 is provided, and the distillation chamber 6 is satisfied to have the oil discharge pipe 14 and the gas discharge pipe 16 so that the structure can be simplified and the volume thereof can be minimized.

또한 본 발명을 이용한 오일의 환원작업시에는 용융기로부터 발생된 기체유기증기가 증류관(2)을 따라 상승하면서 여과실(4)이 갖는 필터(10)의 통과로 기체유기증기중의 불순물이 여과되고, 여과된 기체유기증기는 연통관(8)을 통하여 증류실(6)내에 진입하여 냉각기(13)에 의한 냉각으로 액체화된 오일을 얻게 된다.In addition, during the reduction operation of the oil using the present invention, the gas organic vapor generated from the melter rises along the distillation pipe (2), so that impurities in the gas organic vapor are passed through the filter (10) of the filtration chamber (4). The filtered, filtered gaseous organic vapor enters the distillation chamber 6 through the communication tube 8 to obtain the oil liquefied by cooling by the cooler 13.

상기에 있어, 필터는 8∼15cm두께의 글라스화이바로 구성되는 것으로서, 기체유기증기의 원활한 흐름하에서 불순물의 여과가 이루어지고 또 충분한 여과가 이루어지게 된다.In the above, the filter is composed of a glass fiber bar having a thickness of 8 to 15 cm, the impurities are filtered under sufficient flow of the gas organic vapor and sufficient filtration is performed.

또한 여과실(4)의 통과로 여과된 기체유기증기는 여과실(4)과 증류실(6) 사이에 갖는 연통관(8)과, 상기 연통관(8)과 차단판(12) 사이에 갖는 넓은 틈을 통하여 그 흐름에 방해없이 증류실(6)내부로 유입되고, 증류실내에 유입된 기체유기증기는 계속되는 상승작용으로 유통로(24)를 통한 냉각기(12)의 통과중 냉각으로 액체화되어 낙하하게 되며, 기체유기증기중에 포함된 가스는 그 상부의 가스배출관을 따라 배출된다.In addition, the gas organic vapor filtered through the passage of the filtration chamber 4 has a communication tube 8 provided between the filtration chamber 4 and the distillation chamber 6, and a wide space between the communication tube 8 and the blocking plate 12. The gas is introduced into the distillation chamber 6 without interrupting its flow through the gap, and the gas organic vapor introduced into the distillation chamber is liquefied by cooling during the passage of the cooler 12 through the flow passage 24 in a continuous synergy. The gas contained in the gas organic vapor is discharged along the gas discharge pipe at the upper portion thereof.

또한 냉각기(13)에 의한 냉각으로 액체화되어 낙하하는 오일은 연통관(8)을 차단하는 차단판(12)에 의하여 용융기내에 재유입됨 없이 격판(18) 보다 낮게 형성되는 오일배출관(14)을 통하여 신속하게 회수되는 것이다.In addition, the oil liquefied by the cooling by the cooler 13 falls into the oil discharge pipe 14 formed lower than the diaphragm 18 without being re-introduced into the melter by the blocking plate 12 blocking the communication pipe (8). It is quickly recovered through.

이와 같이 본 발명은 용융기 상부에 연장형성되는 증류관(2)내에 연통관(8) 을 사이에 두고 필터(10)를 갖는 여과실(4)과, 냉각기(13)와 오일배출관(14) 및 가스배출관(16)을 갖는 증류실(6)을 갖도록 하고, 연통관(8) 상부에는 소정간격을 두고 차단판(12)을 갖도록 하는 것으로 만족하므로 구조를 간단히 할 수가 있어 설치비용을 절감할 수가 있고 또 부피의 최소화로 공간활용률을 높여줄 수가 있으며, 기체유기증기의 흐름이 원활하게 이루어질 수가 있고 또 상기 기체유기증기는 냉각기에 의한 냉각시 액체화되면 자중에 의한 낙하로 오일배출관(14)을 통하여 신속히 배출되므로 오일을 얻기까지의 공정 및 시간단축으로 생산성 향상을 가져올 수가 있는 등의 효과가 있는 것이다.As described above, the present invention includes a filtration chamber 4 having a filter 10, a cooler 13, an oil discharge tube 14, and a filter 10 interposed therebetween in a distillation tube 2 extending over the melter. It is satisfied to have a distillation chamber 6 having a gas discharge pipe 16, and to have a blocking plate 12 at a predetermined interval on the communication pipe 8, so that the structure can be simplified and the installation cost can be reduced. In addition, the space utilization rate can be increased by minimizing the volume, and the gas organic vapor can flow smoothly, and when the gas organic vapor is liquefied during cooling by the cooler, the gas organic vapor rapidly falls through the oil discharge pipe 14 due to its own weight. Since it is discharged, it is possible to bring about an improvement in productivity by shortening the process and time until oil is obtained.

Claims (3)

용융기로부터 연장형성되는 증류관의 내측중앙부에 여과실과 증류실을 연통하도록 설치되는 연통관과, 상기 연통관상부에 적정간격을 두고 고정설치되는 차단판과, 여과실내에 설치되는 필터와, 증류실내에 설치되는 냉각기와, 증류실의 일측 하부에 갖는 오일배출관 및 증류실 상부에 갖는 가스배출관으로 구성하여서 된 폐합성수지의 오일환원장치.A communication tube provided to communicate the filtration chamber and the distillation chamber in an inner central portion of the distillation tube extending from the melter, a blocking plate fixedly spaced at an upper portion of the communication tube, a filter installed in the filtration chamber, and a distillation chamber. An oil reduction device for waste synthetic resin composed of a cooler provided, an oil discharge pipe provided at one side lower part of the distillation chamber, and a gas discharge pipe provided at the upper part of the distillation chamber. 청구항1에 있어서, 필터는 상하금속망판사이에 글라스화이바를 약 8∼15cm두께로 충진하여 구성함을 특징으로 하는 폐합성수지의 오일환원장치.The oil reduction device for waste synthetic resin according to claim 1, wherein the filter is formed by filling a glass fiber between about 8 and 15 cm in thickness between upper and lower metal mesh boards. 청구항1에 있어서, 차단판은 연통관의 직경보다 크고 또 단부로 갈수록 하향경사진 형태를 갖도록 구성함을 특징으로 하는 폐합성수지의 오일환원장치.The oil reduction device of the waste synthetic resin according to claim 1, wherein the blocking plate is configured to have a shape larger than the diameter of the communication pipe and downwardly inclined toward the end.
KR1020040058296A 2004-07-26 2004-07-26 Oil reductor waste synthetic resin KR20060009635A (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100743977B1 (en) * 2006-09-25 2007-07-30 임수태 Apparatus for recovering oil
KR20160060902A (en) * 2014-11-21 2016-05-31 이봉희 Heating separator for the separation of metal and resin

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100743977B1 (en) * 2006-09-25 2007-07-30 임수태 Apparatus for recovering oil
KR20160060902A (en) * 2014-11-21 2016-05-31 이봉희 Heating separator for the separation of metal and resin

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