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公开(公告)号：KR1020130045644A
公开(公告)日：2013-05-06
申请号：KR1020110109985
申请日：2011-10-26
Applicant: 한국에너지기술연구원
CPC classification number: Y02W30/62 , C10G1/10 , B09B3/0083 , C08J11/04 , C10B53/07 , C10G2300/1003 , F23G5/027
Abstract: PURPOSE: A pyrolysis process and an operation method thereof are provided to successively operate, to conveniently drive, and to increase thermal efficiency and operating ratio. CONSTITUTION: An operation method of a pyrolysis process comprises the following steps: inserting pre-treated raw materials into a raw material melting bath (13); melting the raw materials by heating exterior wall of the raw material melting bath using a burner or high temperature exhaust gas comes from a pyrolysis reactor (15); measuring the melted raw materials through a melted material measuring tub (14) and adding into the pyrolysis reactor; heating the melted raw materials in the pyrolysis reactor at 350-450 deg. Celsius and pyrolyzing the same; storing liquefied gasoline which is produced by transferring vapor through a wax reduction device (16-1), a gasoline purifier (24) and a condenser(25) in a gasoline collection tank (24); withdrawing sludge after pyrolysis and sending the same to a sludge reactor(18); completely pyrolyzing sludge and forming into powder residue; cooling the powder residue down to approximately 150 deg. Celsius; and repeatedly discharging the cooled residue and storing in the residue collection tank.
Abstract translation: 目的：提供热解过程及其操作方法，以连续操作，方便地驱动和提高热效率和运行率。 构成：热解过程的操作方法包括以下步骤：将预处理的原料插入原料熔融浴（13）; 通过使用燃烧器或高温废气加热原料熔融浴的外壁来熔化原料来自热解反应器（15）; 通过熔化的材料测量池（14）测量熔化的原料并加入到热解反应器中; 在350-450度加热热解反应器中的熔化原料。 摄氏温度; 储存通过将蒸汽通过汽油收集罐（24）中的蜡减少装置（16-1），汽油净化器（24）和冷凝器（25）转移而产生的液化汽油; 热解后取出污泥并将其送至污泥反应器（18）; 完全热解污泥并形成粉末残渣; 将粉末残留物冷却至约150度。 摄氏度; 并重复排出冷却的残渣并储存在残渣收集罐中。
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公开(公告)号：KR101239083B1
公开(公告)日：2013-03-06
申请号：KR1020100030421
申请日：2010-04-02
Applicant: 한국에너지기술연구원
Abstract: 본 발명은 추출탑 내부에 고전압의 전기장을 인가하여 초중질원유 내 아스팔텐을 효과적으로 제거하는 초중질원유의 정제방법 및 정제장치에 관한 것으로, 더욱 상세하게는 탄소수 3~8개의 탄화수소로 구성된 용매와 초중질원유를 혼합하고 이에 고전압의 전기장을 인가하여 초중질원유 내의 아스팔텐 분산 특성을 변화시킴으로써 초중질원유의 응집을 유도하고 이와 동시에 용매와 초중질원유의 접촉을 원활히 하여 용매 추출 효과를 극대화한 다음, 전기장 인가를 중지하여 상부의 아스팔텐 제거 오일 층과 하부의 아스팔텐 층으로 분리시킴으로써 아스팔텐이 제거된 원유를 회수하는 방법 및 장치에 관한 것이다.
즉, 본 발명은 간단한 공정 구성과 온화한 조업 조건을 특징으로 하므로 기존의 탈아스팔텐 용매 추출 공정이 안고 있던 막대한 장치비 및 에너지 다소비 문제를 해결하여 초중질원유 고도화에 소요되는 설치, 운전 비용을 감소할 수 있는 것이다.-
13.发明授权
公开(公告)号：KR101107553B1
公开(公告)日：2012-01-31
申请号：KR1020090107842
申请日：2009-11-10
Applicant: 한국에너지기술연구원
CPC classification number: C07F15/065
Abstract: 본 발명은 2가지 이상의 금속이 결합된 수산화물 계열 전구체의 표면 개질을 통한 유용성(Oil-Soluble) 입자 제조방법에 관한 것이다. 더욱 상세하게는 서로 다른 금속들의 결합으로 이루어진 유용성 입자를 제조하는 것으로, 서로 다른 금속염들을 유기산들과 동시에 혼합하여 유용성 입자로 제조하는 대신에 금속들의 비율 조정 및 제조가 용이한 수산화물 계열 전구체들을 먼저 제조한 후에 유기산들과의 반응을 유도하여 유용성 입자로 제조하는 것을 특징으로 한다.
금속결합 수산화물 계열 전구체, 표면개질, 유용성, 에스테르 반응-
公开(公告)号：KR1020110111588A
公开(公告)日：2011-10-12
申请号：KR1020100030734
申请日：2010-04-05
Applicant: 한국에너지기술연구원
CPC classification number: C10G21/18 , C10G21/02 , C10G2300/1077 , C10G2300/201
Abstract: 본 발명은 특정의 용매인 화학식 1의 용매를 사용하여 상온(15~30)에서 초중질원유를 용해시키고, 극성 유기용매와 비극성 용매를 가함으로써 초중질원유를 경질화하는 방법에 관한 것으로서, 더욱 상세하게는 상온(15~30)에서 오일샌드 비튜멘, 천연역청, 감압잔사유 등의 초중질원유에 특정의 용매 및 극성 유기용매를 가하여, 상부의 아스팔텐 분산제와 극성 유기용매, 레진 성분이 용해된 극성 유기용매층과 하부의 고농축 초중질원유 층으로 분리한 다음, 하부에 탄화수소비극성 유기용매를 가하여 다시 상부의 탈아스팔텐 오일 층과 하부의 아스팔텐 층으로 분리함으로써 초중질원유를 경질화하는 방법에 관한 것이다.
즉, 본 발명은 기존의 초중질원유의 경질화공정이 안고 있던 막대한 장치비 및 에너지 다소비 문제를 해결하여 초중질원유의 경질화에 소요되는 설치, 운전 비용을 감소할 수 있는 것이다.-
公开(公告)号：KR100768690B1
公开(公告)日：2007-10-19
申请号：KR1020060069282
申请日：2006-07-24
Applicant: 한국에너지기술연구원
IPC: C02F11/12
CPC classification number: Y02W10/40 , C02F11/12 , C02F2201/002 , C02F2201/005
Abstract: A sludge injecting apparatus which has a simple structure, and improves the crushing efficiency by intermittently feeding compressed inert gas into a crushing equipment such that sludge is crushed well by an impact of gas applied to the sludge in addition to mechanical crushing of the crushing equipment, and a pyrolysis system having the sludge injecting apparatus are provided. A sludge injecting apparatus comprises: a cylindrical main body(210) including a body consisted of a cylindrical part(212) and a conical tapered part(213), a sludge inflow port(214) and a sludge discharge port(216), and connecting flanges(215,217); an impact generating part(220) which is connected to a lower part of the main body and intermittently generates a gas impact to discharge the gas impact into the main body, the impact generating part including an impact generator(223), a gas inflow pipe(222), and a gas exhaust pipe(227); a first valve(240) which is installed at the sludge inflow port side to control inflow of sludge, and includes a valve plate(241), a traction rack(242), a pinion(243), and a motor(244); and a second valve installed at the sludge discharge port side to control discharge of sludge. The sludge injecting apparatus further comprises an exhaust part(230) including an exhaust pipe(231), a filter part(232), and a sound arrester(235).
Abstract translation: 一种污泥注入装置，其结构简单，并且通过将压缩的惰性气体间歇地进料到破碎设备中，除了破碎设备的机械破碎之外，还通过施加到污泥的气体的冲击将污泥充分压碎，从而提高了破碎效率， 并设有具有污泥注入装置的热解系统。 污泥注入装置包括：圆筒形主体（210），包括由圆柱形部分（212）和锥形锥形部分（213）组成的主体，污泥流入口（214）和污泥排出口（216），以及 连接法兰（215,217）; 冲击产生部件，其连接到主体的下部并间歇地产生气体冲击以将气体冲击排放到主体中，该冲击产生部件包括冲击发生器，气体流入管 （222）和排气管（227）; 第一阀（240），其安装在污泥流入口侧以控制污泥的流入，并且包括阀板（241），牵引架（242），小齿轮（243）和马达（244）; 以及安装在污泥排出口侧的第二阀，以控制污泥的排放。 污泥注入装置还包括排气部（230），其包括排气管（231），过滤部（232）和防声器（235）。
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Patent Agency Ranking
公开(公告)号：KR100736845B1
公开(公告)日：2007-07-10
申请号：KR1020060081825
申请日：2006-08-28
Applicant: 한국에너지기술연구원
Abstract: A fuel oil refining device and a pyrolysis system having the same are provided to improve the quality of fuel oil by successively passing various impurities and harmful gas included in the fuel oil distilled in a distillation tower through plural refining tanks. In the pyrolysis system, the fuel oil refining device(200) is composed of a first refining tank(10) for receiving fuel oil including impurities and filtering large particles of the fuel oil through an envelop-shaped bag filter; a second refining tank(20) for filtering fine particles of the fuel oil refined in the first refining tank by a first rod-shaped cartridge filter installed inside; a third refining tank(30) for filtering hyperfine particles and moisture of the fuel oil refined in the second refining tank by second and third cartridge filters installed inside; and a fourth refining tank(40) receiving the fuel oil refined in the third refining tank and filtering harmful chemical components by passing the fuel oil through a fourth cartridge filter made of carbons.
Abstract translation: 本发明提供一种燃料油精制装置及具备该燃料精制装置的热分解系统，通过使在蒸馏塔内馏出的燃料油中含有的各种杂质和有害气体依次通过多个精制槽而提高燃料油的品质。 在热解系统中，燃料油精制装置（200）由第一精制罐（10）和第二精制罐（10）组成，所述第一精炼罐用于接收包含杂质的燃料油并通过封套式袋式过滤器过滤燃料油的大颗粒。 第二精制槽（20），用于通过设置在内部的第一棒状筒式过滤器过滤在第一精制槽中精炼的燃料油的微粒; 第三精制罐（30），用于通过安装在第二精炼罐内的第二和第三筒式过滤器过滤在第二精炼罐中精炼的燃料油的超细颗粒和水分; 和第四精制罐（40），其接收在第三精炼罐中精炼的燃料油，并通过使燃料油通过由碳制成的第四筒式过滤器来过滤有害化学成分。
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公开(公告)号：KR1020140058979A
公开(公告)日：2014-05-15
申请号：KR1020120125511
申请日：2012-11-07
Applicant: 한국에너지기술연구원
CPC classification number: B01J8/1872 , C10J3/48
Abstract: The present invention relates to an indirect gasifier with a dual bubbling fluidized bed. The indirect gasifier comprises: a first bubbling fluidized bed reactor (100) including a gasification area (110) in which materials to be gasified are fed and gasified to be discharged as a synthetic gas; and a second bubbling fluidized bed reactor (200) that is installed adjacent to the first bubbling fluidized bed reactor (100) with a wall (300) therebetween and includes a combustion area (210) in which materials to be combusted are fed and combusted to be discharged as a combusted gas. A fluid sand transferring device (400) is installed on the wall (300) so as to move the gasification area (110) and combustion area (210), so that heat that is generated during combustion in the combustion area (210) is transferred to the gasification area (110). According to the configuration of the present invention, fluid sand is circulated by being horizontally moved in two bubbling fluidized bed reaction areas so that heat that is generated during combustion is transferred to the gasification area (110) and raw materials, which are fed in the indirect gasifier, are gasified. Fluid sand can be horizontally circulated so that the indirect gasifier can be stably and easily operated.
Abstract translation: 本发明涉及具有双重鼓泡流化床的间接气化器。 间接气化器包括：第一鼓泡流化床反应器（100），其包括气化区域（110），其中待气化的材料被气化并气化以作为合成气体排出; 和与第一鼓泡流化床反应器（100）相邻的第二鼓泡流化床反应器（200），其间具有壁（300），并且包括燃烧区域（210），其中待燃烧的材料被进料并燃烧至 作为燃烧气体排放。 流体砂输送装置（400）安装在壁（300）上，以便移动气化区（110）和燃烧区（210），使得在燃烧区域（210）中的燃烧期间产生的热量被转移 到气化区域（110）。 根据本发明的结构，流体砂通过在两个鼓泡流化床反应区域中水平移动而循环，使得在燃烧期间产生的热量被转移到气化区域（110）和原料 间接气化器气化。 流砂可以水平循环，使得间接气化器可以稳定和容易地操作。
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公开(公告)号：KR101130337B1
公开(公告)日：2012-03-26
申请号：KR1020100039928
申请日：2010-04-29
Applicant: 한국에너지기술연구원
Abstract: 본 발명은 생활계 혼합 폐플라스틱을 열분해하여 생성된 저급 왁스 오일을 제올라이트계 촉매 존재하에서 열분해하여 고급 탄화수소로 전환시키는 방법에 관한 것이다.
보다 구체적으로, 본 발명은 폴리올레핀계가 주성분인 필름유의 혼합 폐플라스틱을 고온의 상용 로터리 킬른(rotary kiln) 반응 장치에서 열분해하여 얻은 왁스 오일을 제올라이트계 촉매하에서 열분해하여 탄소수 5개 내지 40개인 고급 탄화수소로 전환시키는 방법에 관한 것이다.-
公开(公告)号：KR1020110120493A
公开(公告)日：2011-11-04
申请号：KR1020100039928
申请日：2010-04-29
Applicant: 한국에너지기술연구원
Abstract: PURPOSE: A transforming method of wax oil obtained by hydrolyzing waste plastic into high class light oil is provided to catalyst-decomposing the wax oil using a zeolite based catalyst. CONSTITUTION: A transforming method of wax oil obtained by hydrolyzing waste plastic into high class light oil comprises a step of hydrolyzing the waste plastic to obtain the low class wax oil with 5-40 carbons including normal paraffin and normal olefin as main components at 350-450 deg C, under the presence of a zeolite based catalyst. The zeolite based catalyst is a ZSM-5 catalyst or a zeolite Y catalyst.
Abstract translation: 目的：提供通过将废塑料水解成高级轻油而获得的蜡油的转化方法，使用沸石型催化剂催化分解蜡油。 构成：通过将废塑料水解成高级轻油而获得的蜡油的转化方法包括水解废塑料以获得具有5-40个碳的低级蜡油的步骤，包括正构链烷烃和正常烯烃作为主要成分， 450℃，在沸石基催化剂存在下。 基于沸石的催化剂是ZSM-5催化剂或沸石Y催化剂。
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公开(公告)号：KR1020110075308A
公开(公告)日：2011-07-06
申请号：KR1020090131725
申请日：2009-12-28
Applicant: 한국에너지기술연구원
CPC classification number: Y02W30/703
Abstract: PURPOSE: A continuous processing method of a batch type process for producing recycled fuel oil from waste plastic is provided to convert a batch type thermal cracking process into a continuous thermal cracking process by adding some apparatuses to the batch type thermal cracking process and remodeling a conventional apparatus. CONSTITUTION: A continuous processing method of a batch type process for producing recycled fuel oil from waste plastic comprises the steps of: transferring residue sludge stacked in a thermal cracking step to a sludge reactor(9); leaving the powdery residue at the back end of the sludge reactor and transferring the residue to a residue transfer device(10) by thermally cracking the transferred sludge in the sludge reactor at a temperature of 410 - 460°C; and transferring the residue to a cooling device(12) through the residue transfer device and storing the cooled residue in a storage device(13).
Abstract translation: 目的：提供一种用于从废塑料生产回收燃料油的间歇式方法的连续加工方法，通过向批式热裂解工艺添加一些装置并将常规 仪器。 构成：用于从废塑料生产回收燃料油的间歇式方法的连续加工方法包括以下步骤：将在热裂解步骤中堆叠的残渣污泥转移至污泥反应器（9）; 在污泥反应器的后端留下粉末残留物，并通过在410-460℃的温度下对污泥反应器中转移的污泥进行热裂化将残余物转移到残余物转移装置（10）; 并通过残余物转移装置将残余物转移到冷却装置（12），并将冷却的残余物储存在存储装置（13）中。
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