KR100699519B1 - Circulating fluidized bed boiler for combustion of waste and RPF - Google Patents

Circulating fluidized bed boiler for combustion of waste and RPF Download PDF

Info

Publication number
KR100699519B1
KR100699519B1 KR1020050109232A KR20050109232A KR100699519B1 KR 100699519 B1 KR100699519 B1 KR 100699519B1 KR 1020050109232 A KR1020050109232 A KR 1020050109232A KR 20050109232 A KR20050109232 A KR 20050109232A KR 100699519 B1 KR100699519 B1 KR 100699519B1
Authority
KR
South Korea
Prior art keywords
combustion
heat exchanger
rpf
fuel
fluidized bed
Prior art date
Application number
KR1020050109232A
Other languages
Korean (ko)
Inventor
선도원
박재현
이창근
진경태
배달희
조성호
최용준
김유석
황재동
류지원
Original Assignee
한국에너지기술연구원
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 한국에너지기술연구원 filed Critical 한국에너지기술연구원
Priority to KR1020050109232A priority Critical patent/KR100699519B1/en
Application granted granted Critical
Publication of KR100699519B1 publication Critical patent/KR100699519B1/en

Links

Images

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/46Recuperation of heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00Fluidised bed combustion apparatus
    • F23C10/02Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed
    • F23C10/04Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone
    • F23C10/08Fluidised bed combustion apparatus with means specially adapted for achieving or promoting a circulating movement of particles within the bed or for a recirculation of particles entrained from the bed the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone characterised by the arrangement of separation apparatus, e.g. cyclones, for separating particles from the flue gases
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D1/00Burners for combustion of pulverulent fuel
    • F23D1/02Vortex burners, e.g. for cyclone-type combustion apparatus
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/44Details; Accessories
    • F23G5/48Preventing corrosion
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2202/00Combustion
    • F23G2202/10Combustion in two or more stages
    • F23G2202/106Combustion in two or more stages with recirculation of unburned solid or gaseous matter into combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2206/00Waste heat recuperation
    • F23G2206/20Waste heat recuperation using the heat in association with another installation
    • F23G2206/203Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G2900/00Special features of, or arrangements for incinerators
    • F23G2900/00001Exhaust gas recirculation
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Fluidized-Bed Combustion And Resonant Combustion (AREA)

Abstract

A circulating fluidized bed boiler for combustion of waste and RPF(Refused Plastic Fuel) is provided to improve energy recovery efficiency by making sewage slurry and waste plastic into RPF and supplying the RFP as fuel for an energy generating boiler. A circulating fluidized bed boiler for combustion of waste and RPF includes a cyclone(4), a circulation heat transfer member(7), an absorbing tower(9), a back filter(10), and a cleaning tower(11). A seal pot(5) is installed on the bottom side of the cyclone by supplying the fuel stored in a fuel reservoir(1) to a combustion furnace(3) connected to a fuel insertion device(2). An external heat exchanger(6) is connected to the top side and the circulation heat transfer member is connected to a center. A particle material circulation path(22) connects the seal pot to the external heat exchanger. A final over heating device(28) is installed inside the circulation heat transfer member and the external heat exchanger.

Description

폐기물과 알피에프 연소 전용 순환유동층 보일러{Circulating fluidized bed boiler for combustion of waste and RPF}Circulating fluidized bed boiler for combustion of waste and RPF}

도 1 은 본 발명의 바람직한 실시예를 나타낸 슬러지 혼합 RPF연소 전용 순환유동층 보일러의 설치상태도1 is a state diagram of the installation of sludge mixed RPF combustion dedicated circulating fluidized bed boiler showing an embodiment of the present invention

도 2 는 본 발명의 슬러지 혼합 RPF연소 전용 순환유동층 보일러의 일부 단면도2 is a partial cross-sectional view of the sludge mixed RPF combustion dedicated circulating fluidized bed boiler of the present invention

도 3 은 본 발명의 도 2 에 대한 측면도3 is a side view of FIG. 2 of the present invention;

[도면의 주요 부분에 대한 부호의 설명][Description of Symbols for Main Parts of Drawing]

1 : 연료 저장조 2 : 연료 투입기 1: fuel reservoir 2: fuel injector

3 : 연소로 4 : 싸이클론 3: combustion furnace 4: cyclone

5 : 시일포트 6 : 외부열교환기 5: seal port 6: external heat exchanger

7 : 대류 전열부 8 : 압입송풍기 7: convection heat transfer unit 8: press-in blower

9 : 흡수탑 10 : 백필터 9: absorption tower 10: bag filter

11 : 세정탑 12 : 유인송풍기 11: washing tower 12: manned blower

13 : 굴뚝 20 : 드럼 13: chimney 20: drum

21, 22 : 입자재순환로 23 : 입자이송로21, 22: particle recirculation path 23: particle transfer path

24 : 강수관(down comer) 25 : 절탄기(economizer) 24: down comer 25: economizer

26 : 1차 슈퍼히터(super heater) 27 : 2차 슈퍼히터  26: 1st super heater 27: 2nd super heater

28 : 최종과열기(3차 슈퍼히터) 29 : 공기예열기 28: final superheater (3rd super heater) 29: air preheater

30 : 급수관(feed water pipe) 31 : 증기배출관(steam out pipe)  30: feed water pipe 31: steam out pipe

본 발명은 가연성 폐기물이나 건조 슬러지, 폐플라스틱 등으로부터 만들어진 고형연료 RDF 또는 RPF를 새로운 개념의 순환유동층 열병합 보일러에서 연료를 안전하게 연소하고 고효율로 에너지를 회수하고자 하는 것으로,The present invention seeks to safely burn fuel and recover energy with high efficiency from solid fuel RDF or RPF made from flammable waste, dry sludge, waste plastic, etc. in a new concept circulating fluidized bed cogeneration boiler.

더욱 상세하게는 순환유동층 기술을 이용하여 휘발분이 많고 발열량이 높은 RDF 및 RPF 연료를 노의 과열 없이 연소하며, 산성가스 분위기인 폐기물 연료 연소분위기에서 본 발명의 고유한 비기계적 입자 순환장치를 사용하여 입자를 연소로와 외부 열교환기로 순환하고 최종 과열기의 부식을 억제하기 위하여 최종 과열기를 외부 열교환기에 배치하여 고효율 연소와 부식 방지 기능이 완벽한 새로운 고체연료 연소 순환유동층 연소로와 보일러로서 전기나 열을 공급하는 장치에 관한 것이다.More specifically, RDF and RPF fuels having high volatility and high calorific value are burned without overheating of the furnace by using a circulating fluidized bed technology, and the non-mechanical particle circulator of the present invention is used in a waste fuel combustion atmosphere in an acid gas atmosphere. The final superheater is placed in the external heat exchanger to circulate the particles to the combustion furnace and external heat exchanger and to suppress the corrosion of the final superheater, supplying electricity or heat as a new solid fuel combustion circulation fluidized bed combustion furnace and boiler with high efficiency combustion and corrosion protection. It relates to a device to.

국내에 도입되어 가동 중이거나 검토 중인 소각 기술에는 스토커 방식 이외에 슬러지를 대상으로 하는 플라즈마 소각 방식과 용융소각 방식 등이 있다. 이러한 소각 방식은 폐기물의 유해성 여부에 상관없이 일괄처리 공정으로 진행되고 안전성 확보를 위한 처리비용 발생으로 운전비가 높은 단점이 있다. Incineration technologies that have been introduced and are in operation or under consideration in Korea include the plasma incineration method and the sludge incineration method for sludge, in addition to the stocker method. This incineration method has a disadvantage in that the operation cost is high due to the processing cost for ensuring the safety and proceeds in a batch processing process regardless of the harmfulness of the waste.

일부 연구기관이나 학교 등에서 공정개발 연구를 수행하고 있으나 아직은 소각 장치의 설계와 운전, 대형화 기술에 있어서 실증과 기술검증이 필요한 상황이다. 재생연료에 관한 기술 또한 현행법상 폐기물로 분류되는 RDF에 관한 제조기술 정도이다. RDF(Refuse Derived Fuel)에 관한 법 규정이 마련되어 있지 않기 때문에 폐기물 소각설비에서 연소하여야 한다. Although some research institutes and schools are conducting process development research, there is still a need for demonstration and technical verification in the design, operation, and large-scale technology of incineration. Renewable fuel technology is also a manufacturing technology for RDF that is classified as waste under current law. Since there are no statutory provisions regarding the use of recycle derived fuel (RDF), it must be combusted in a waste incineration plant.

제조환경에서 염소성분이 과다해질 경우 연료 사용량에 제한을 받아 고온 스팀 회수가 어려워질 가능성이 있으며, 설비의 특성상 산업지역이나 인구밀집지역 설치시 제약을 받게 된다.Excessive chlorine in the manufacturing environment may limit the use of fuel, making it difficult to recover high-temperature steam. Due to the nature of the facility, it is restricted when installing industrial or densely populated areas.

특허 2002-0066539 호 '폐기물 고형연료 소각장치를 이용한 온수 및 온풍공급시스템(2002.08.19)'의 경우 고정층에서 1차연소실과 2차연소실을 갖는 온수 및 난방용 열공급을 하며, 공해방지시설을 갖추지 않은 단순한 소형시스템이나 본 발명의 경우 순환유동층을 이용한 증기 또는 전기생산을 목적으로 대형 산업용보일러로서 고유한 비기계적 입자 순환장치를 사용하여 입자를 연소로와 외부 열교환기로 순환하고 최종과열기의 부식을 억제하기 위하여 최종과열기를 외부 열교환기에 배치하여 고효율 연소와 부식 방지 기능이 완벽한 새로운 고체연료 연소 순환유동층 연소로와 보일러로서 전기나 열을 공급하는 장치이다. 고정층에서 1차 연소실과 2차 연소실을 가지며 온수 및 난방용 열을 공급하는 공해방지시설이 갖춰지지 않은 단순한 소형 시스템이다.Patent 2002-0066539 'Hot and hot air supply system using waste solid fuel incinerator (2002.08.19)' is a simple bed that does not have pollution prevention facilities and supplies heat for hot water and heating with primary combustion chamber and secondary combustion chamber in a fixed bed. In the case of a small system or the present invention, using a unique non-mechanical particle circulation device as a large industrial boiler for the production of steam or electricity using a circulating fluidized bed, the particles are circulated to a combustion furnace and an external heat exchanger and the corrosion of the final superheater is suppressed. The superheater is placed in an external heat exchanger to supply electricity or heat as a new solid fuel combustion circulating fluidized bed combustor and boiler with perfect high efficiency combustion and corrosion protection. It is a simple compact system with a primary combustion chamber and a secondary combustion chamber in a fixed bed and no pollution prevention facilities that supply hot water and heat for heating.

특허 2002-0061283 호 '고형연료용 소각 보일러(2002.07.24)'의 경우 케이스의 내측면에 단열벽돌을 설치하고 에어노즐이 구비된 냉각관, 로내의 바닥 및 벽에 열교환기를 설치하여 소규모 온수의 공급 혹은 난방을 목적으로 하는 공해방지시설이 갖춰지지 않은 단순한 소형 시스템이다. Patent 2002-0061283 'Incineration Boiler for Solid Fuel (2002.07.24)' installs a thermal insulation brick on the inner side of the case and installs a heat pipe on the bottom and wall of the cooling pipe equipped with an air nozzle, It is a simple compact system with no pollution prevention facilities for supply or heating.

본 발명은 하수종말처리장에서 배출되는 하수 슬러지를 생활계나 사업장의 폐플라스틱과 함께 혼합한 후 고형화하여 제조한 RPF를 새로운 개념의 순환유동층 열병합 보일러에서 연소하여 고효율로 에너지를 회수하고 공해방지 기술을 극대화하여 폐기물의 사용을 안전하게 하는데 목적이 있다.The present invention is to mix the sewage sludge discharged from the sewage terminal treatment plant with the waste plastic of the living or workplace and to solidify the RPF produced in a new concept circulating fluidized bed cogeneration boiler to recover energy with high efficiency and maximize pollution prevention technology The purpose is to secure the use of waste.

본 발명은 배연제어와 전열관의 부식방지 기능이 완벽한 새로운 국산 고체연료 연소용 순환유동층 보일러에서 완전연소를 실증하여 증기에 의해 생성된 전기나 열을 공급하는 장치에 관한 것으로, 고유한 비 기계적 입자 순환장치를 사용하여 입자를 연소로와 외부 열교환기로 순환시키고 최종 과열기를 외부 열교환기에 배치함으로써 최종 과열기의 부식을 억제하는 대형산업용 보일러에 관한 것이다. The present invention relates to a device for supplying electricity or heat generated by steam by demonstrating complete combustion in a new domestic solid fuel combustion circulating fluidized bed boiler with perfect flue gas control and corrosion protection of a heat pipe. A large industrial boiler which uses a device to circulate particles into a combustion furnace and an external heat exchanger and places the final superheater in an external heat exchanger to suppress corrosion of the final superheater.

본 발명은 환경공해물질 배출을 비롯한 유해성이 적은 폐플라스틱과 하수 슬러지를 대상으로 일반 시설에서 수송과 보관이 가능하고 일반 고체연소 보일러에서 제한적으로 연소 열 이용이 가능한 RPF(Refused Plastic Fuel)를 가장 경제적인 방법으로 생산하며 이를 안전하게 소각하고 에너지 이용을 극대화 할 수 있는 신개념의 순환유동층 공정을 개발할 뿐 아니라 이를 실증하여 바로 국산화 상용화 할 수 있게 함을 특징으로 한다.The present invention is the most economical for RPF (Refused Plastic Fuel) that can be transported and stored in a general facility for limited waste plastics and sewage sludge, including environmental pollutants discharge, and limited combustion heat available in a general solid combustion boiler In addition to developing a new concept of circulating fluidized bed process that can be produced by phosphorus method and safely incinerated and maximizing energy use, it can be immediately localized and commercialized.

본 발명의 유동층 소각은 전 세계적으로 슬러지 처리방안으로 점차 증가하는 추세에 있는데 이는 다음과 같은 이점이 있기 때문이다. Fluidized bed incineration of the present invention is gradually increasing as a sludge treatment method worldwide, because it has the following advantages.

첫째 층내 혼합이 잘 되기 때문에 상대적으로 낮은 온도와 과잉공기율에서도 완전 연소가 가능하다. First, because of good mixing within the bed, complete combustion is possible at relatively low temperatures and excess air rates.

둘째 많은 양의 층내 불활성 물질이 열 저장소의 역할을 하여 갑작스러운 온도 변화를 방지해준다. Second, a large amount of inert material in the layer acts as a heat reservoir to prevent sudden temperature changes.

셋째 층내의 적은 양의 연료나 석탄은 연소로가 조업온도 근처에 있을 때 스타트-업(start-up)이나 스타트-다운(shut-down)을 수분 내에 가능하게 해준다. Small amounts of fuel or coal in the third bed allow for start-up or shut-down in minutes when the furnace is near operating temperature.

넷째 많은 양의 층물질은 열 충격에 따른 내화물의 손상을 줄이고 또한 소각로의 고온 부분에 무빙 파트(moving part)가 없기 때문에 보수 유지비가 적게 든다. 또한 유동층 소각로는 반응기의 열전달이 우수할 뿐 아니라 별도의 공정 없이도 공해물질의 배출억제가 가능하고 수분을 많이 포함하고 있는 연료에도 적응이 뛰어나다는 장점이 있어 다양한 분야에서 적용되고 있다. 특히 외부 열교환식 순환유동층 방식을 도입할 경우 최종 과열기의 부식을 억제할 수 있어 연소로 관리에 매우 효과적이다.Fourth, a large amount of layer material reduces the damage of the refractory due to thermal shock and also low maintenance costs because there is no moving part in the hot part of the incinerator. In addition, the fluidized bed incinerator is applied in various fields because it not only has excellent heat transfer in the reactor, but also has the advantage of being able to suppress the emission of pollutants without a separate process and adapting it to fuel containing a lot of water. In particular, when the external heat exchange type circulating fluidized bed system is introduced, the corrosion of the final superheater can be suppressed, which is very effective in the management of the combustion furnace.

본 발명은 종래의 단순 소각방법으로는 열 회수를 할 수 없고 스토카 등의 폐열 보일러는 폐기물의 열량변화에 대응하기 어려우며 완전연소와 환경관리가 어렵다는 점과 발생 스팀의 온도가 낮아 효율적인 에너지 이용이 불가능하다는 점을 개선하여 외부 열 교환식 순환유동층 연소방식을 독자적으로 개발하여 고효율 연소와 철저하고도 경제적인 배연제어 및 고온의 스팀회수가 가능하며 더욱이 산성 가스에 의한 보일러 수관의 부식을 최소한으로 억제할 수 있다. 또한 이 방식은 보일러의 온도관리가 용이하여 부하조절과 운전관리 성능도 탁월하다.The present invention can not recover the heat by the conventional simple incineration method, waste heat boilers such as stoka is difficult to cope with changes in the heat of the waste, it is difficult to completely burn and environmental management, and the temperature of the generated steam is low and efficient use of energy Independently developed external heat exchange type circulating fluidized bed combustion system by improving the impossibility to enable high efficiency combustion, thorough and economical flue gas control, high temperature steam recovery, and further minimize the corrosion of boiler water pipe by acid gas. Can be. In addition, this method is easy to control the temperature of the boiler, so the load control and operation management performance is excellent.

이하에서 본 발명의 바람직한 실시예를 첨부 도면에 따라 상세하게 설명하기로 한다.Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

RPF를 저장하는 연료 저장조(1)의 하측으로 연료를 정량 투입하는 연료공급장치(2)를 설치하고, 이 연료공급장치(2)에서 연소로(3)에 일정량의 고체 유동물질을 투입하도록 한다.A fuel supply device 2 for quantitatively injecting fuel is installed under the fuel storage tank 1 storing the RPF, and the fuel supply device 2 is configured to inject a certain amount of solid flow material into the combustion furnace 3. .

상기 연소로(3)에는 유인송풍기(12)와 압입송풍기(8)를 가동하여 유동화시키도록 한다.The combustion furnace 3 is operated to fluidize the manned blower 12 and the press-fit blower (8).

상기 연소로(3)의 내부에는 수관이 설치되거나 공간을 형성하여 놓고, 상측에서 싸이클론(4)과 연결되어 있으며, 싸이클론(4)의 하측에는 시일포트(5)가 연결되어 있다.The water pipe is installed inside the combustion furnace 3 or forms a space, and is connected to the cyclone 4 from the upper side, and the seal port 5 is connected to the lower side of the cyclone 4.

상기 시일포트(5)는 입자재순환로(21, 22)가 각각 양측으로 분리되어 있어서 입자재순환로(21)는 입자이송로(23)와 연결되어 연소로(3)에 연결되며, 입자재순환 로(22)는 외부 열교환기(6)와 연결되어 있다.The seal port 5 has particle recirculation paths 21 and 22 separated on both sides, so that the particle recirculation path 21 is connected to the particle transfer path 23 and connected to the combustion furnace 3. 22 is connected to the external heat exchanger 6.

상기 외부 열교환기(6)는 기계적 차단(제어) 장치가 설치되지 않고 연소로(3)의 상황에 따라서 재순환되어 연소할 연료가 투입되도록 한다.The external heat exchanger 6 is recycled according to the situation of the combustion furnace 3 without a mechanical shutoff (control) device to allow fuel to be burned.

상기 싸이클론(4)에는 대류전열부(7)를 연결하며 압입송풍기(8)와 흡수탑(9)이 연결되며, 흡수탑(9)에서 연속으로 백필터(10)와 세정탑(11), 유인송풍기(12) 및 굴뚝(13)이 설치된다.The cyclone (4) is connected to the convection heat exchanger (7), the press-in blower (8) and the absorption tower (9) is connected, the bag filter 10 and the cleaning tower (11) in a continuous absorption tower (9) , Manned blower 12 and the chimney 13 is installed.

상기 스팀드럼(20)에는 연소로(3)와 대류전열부(7)로 연결되고, 하측으로 강수관(down comer pipe)(24)가 연결되며, 일측으로 급수관(FEED WATER PIPE)(30) 및 증기배출관(STEAM OUTLET PIPE)(31)가 연결되어 있다.The steam drum 20 is connected to the combustion furnace 3 and the convection heat exchanger 7, and a down comer pipe 24 is connected to the lower side of the steam drum 20, and a feed water pipe 30 is connected to one side of the steam drum 20. And a steam outlet pipe 31 is connected.

연소로(3)에 일정량의 고체 유동물질을 투입하고 유인송풍기(12)와 압입송풍기(8)를 가동하여 유동화시키며, 고체 예열버너를 가동하여 고체 유동물질의 온도가 RPF 연소조건에 도달하면 연료 저장조(1)에 저장된 RPF를 연료공급장치(2)를 통하여 정량적으로 투입하면 원활한 연소가 가능하다. 이때 고체 일부와 회재는 기체와 같이 비말 동반하여 싸이클론(4)에서 포집되어 시일포트(5)와 외부 열교환기(6)를 거쳐 연소로(3)로 재순환하며, 기체와 미세입자는 대류 전열부(7), 흡수탑(9), 백필터(10), 세정탑(11)을 거쳐 굴뚝을 통해 배출된다.A certain amount of solid fluid is introduced into the combustion furnace 3, and the manned blower 12 and the press-fit blower 8 are operated to fluidize. When the solid preheat burner is operated, the temperature of the solid fluid reaches the RPF combustion condition. If the RPF stored in the reservoir 1 is quantitatively injected through the fuel supply device 2, smooth combustion is possible. At this time, a part of the solid and ash are collected in the cyclone (4) accompanied by a droplet like gas, and recycled to the combustion furnace (3) through the seal port (5) and the external heat exchanger (6), and the gas and the fine particles are convective heat transfer. The part 7, the absorption tower 9, the bag filter 10, and the washing tower 11 are discharged through the chimney.

한편 열회수를 위한 공정은 전 처리된 물은 펌프(도시하지 않음)를 통해 절탄기(Economizer)(25)를 거쳐 스팀드럼(20)에서 강수관(24) 로 내려와 다시 연소로(3) 벽에 설치된 수관을 통해 이동하면서 열전달 현상에 의해 스팀으로 상(phase) 변화되어 스팀드럼(20)으로 순환한다. On the other hand, the process for the heat recovery is the pre-treated water is passed down from the steam drum (20) to the downcomer (24) through the economizer (25) through a pump (not shown) to the wall of the furnace 3 again While moving through the installed water pipe, the phase changes to steam by heat transfer and circulates to the steam drum 20.

스팀은 스팀드럼(20) 상부에서 나와 1차 슈퍼히터(26), 2차 슈퍼히터(27), 3차 슈퍼히터(28)를 거치며 일정온도와 압력을 갖는다. 이 스팀을 이용하여 전기 생산 및 열회수 공정을 통해 에너지로 활용한다. 특히 일반적으로 스팀드럼(20)에서 나온 후 스팀의 과열과정에서 수관이 HCl과 반응하여 고온 부식을 일으키는 450도 이상에서 HCl과의 직접 접촉이 되지 않게 하기 위하여 최종 과열기(28)를 외부 열교환기(6)에 설치한 것이다. Steam comes out of the steam drum 20, the first super heater 26, the second super heater 27, the third super heater 28 and has a constant temperature and pressure. This steam is used as energy through electricity production and heat recovery processes. In particular, in order to prevent direct contact with HCl at a temperature above 450 degrees where the water pipe reacts with HCl and causes high temperature corrosion during steam overheating after exiting the steam drum 20. 6) is installed.

고온 부식을 일으키는 부식성 물질이 대류전열부(7)를 통하여 흡수탑(9)으로 이동되며 최종 과열기(28)를 외부 열교환기(6)에 설치함으로써 외부 열교환기(6)에서는 직접 접촉을 하지 않도록 하므로 부식을 염려할 필요가 없는 것이다.Corrosive substances causing high temperature corrosion are transferred to the absorption tower 9 through the convection heat exchanger 7 and the final superheater 28 is installed in the external heat exchanger 6 so that the external heat exchanger 6 is not in direct contact. Therefore, there is no need to worry about corrosion.

본 발명은 하수 슬러지와 폐플라스틱을 RPF로 재이용함으로써 효율적이고 환경친화적인 자원순환이 가능하고, 종래의 소각로 연소에서 벗어나 고체연료보일러에서 연료로 활용함은 물론 해양오염 저감효과, 매립지 수명연장이 가능하며, 기술적 파급효과는 기존의 외국 기술과 차별화되는 온도조절 및 관리기능이 뛰어나고 부식에 강한 국산 순환유동층 RPF 연소보일러의 개발과 실증 소각보일러와 차별되어 주거환경이나 산업장에 설치하여 에너지 이용이 가능하다.The present invention enables efficient and environmentally friendly resource circulation by reusing sewage sludge and waste plastics as RPF, and can be used as a fuel in solid fuel boilers as well as to reduce marine pollution and extend landfill life, away from the conventional incinerator combustion. The technical ripple effect is excellent in temperature control and management function that is differentiated from the existing foreign technology and development of domestic circulating fluidized bed RPF combustion boiler resistant to corrosion and differentiated from demonstration incineration boiler can be installed in a residential environment or industrial place to use energy. Do.

본 발명은 경제적 파급효과는 하수 슬러지와 폐 플라스틱을 이용해 고형 연료화(RPF)하여 발전용 보일러의 연료로 공급하여 대체 에너지로 사용함으로써 에너지 대체 효과가 크고, 연소 열 이용을 통해 에너지를 회수함으로서 경제성 확보가 가능하다.In the present invention, the economic ripple effect is solid fueled by using sewage sludge and waste plastics (RPF) and supplied as a fuel of a power generation boiler to be used as an alternative energy, thereby ensuring greater energy replacement effect and recovering energy through the use of combustion heat. Is possible.

본 발명은 최종 과열기를 외부열교환기에 설치함으로써 450도이상에서 HCL과 직접 접촉되는 것을 방지하므로 고온부식을 원천 방지하는 것이다.The present invention prevents direct contact with the HCL by more than 450 degrees by installing the final superheater in the external heat exchanger to prevent high temperature corrosion.

Claims (4)

연료 저장조(1)에 저장된 연료를 하측의 연료 투입기(2)와 연결한 연소로(3)에 공급하여 연소시키어 하측에 시일포트(5)를 설치한 싸이클론(4)과 상측에서 그리고 중앙에서 외부열교환기(6)와 대류전열부(7)가 연결되며 이 대류전열부(7), 흡수탑(9), 백필터(10), 세정탑(11)을 거쳐 굴뚝을 통해 배출되는 순환유동층 보일러에 있어서,The fuel stored in the fuel reservoir 1 is supplied to the combustion furnace 3 connected to the lower fuel injector 2 and combusted, and the cyclone 4 having the seal port 5 installed on the lower side and above and in the center thereof. Circulating fluidized bed discharged through the chimney through the external heat exchanger (6) and the convection heat exchanger (7) and the convection heat exchanger (7), absorption tower (9), bag filter (10), cleaning tower (11) In the boiler, 상기 시일포트(5)와 외부 열 교환기(6)를 입자재순환로(22)가 연결하며, 상기 대류전열부(7)와 외부 열 교환기(6)의 내부에 설치한 최종 과열기(28)가 연결됨을 특징으로 하는 폐기물과 RPF 연소 전용 순환유동층 보일러.A particle recirculation path 22 connects the seal port 5 and the external heat exchanger 6, and a final superheater 28 installed inside the convection heat exchanger 7 and the external heat exchanger 6 is connected. Circulating fluidized bed boiler dedicated to waste and RPF combustion. 제1항에 있어서,The method of claim 1, 시일포트(5)는 RPF 연소를 위한 고체의 유량이 공기를 제어하는 유량계의 기체량에 따라 비례하여 기계적 장치가 없이 비 기계적으로 조절되며 연소로로 재순환되는 기체의 양과 고체의 온도차이에 따라 연소상태의 개선 및 연소로(3)의 온도조절이 가능함을 특징으로 하는 폐기물과 RPF 연소 전용 순환유동층 보일러.The seal port 5 is non-mechanically controlled without a mechanical device in proportion to the amount of gas in the flow rate controlling the air for the RPF combustion, and is burned according to the temperature difference between the amount of gas recycled to the combustion furnace and the solid. Waste and RPF combustion circulating fluidized bed boiler, characterized in that the improved condition and the temperature control of the furnace (3). 제1항에 있어서,The method of claim 1, 시일포트(5)는 PRF 연소를 위한 고체의 유량이 공기를 제어하는 유량계의 기체량에 따라 비례하여 기계적 장치가 없이 비 기계적으로 조절되며 입자재순환로(21, 22)가 각각 양측으로 분리되어 있어서 입자재순환로(21)로 입자이송로(23)와 연결되어 연소로(3)에 연결하며, 입자재순환로(22)는 외부 열교환기(6)와 연결되고 시일포트(5)에 남아 있는 고체가 연소로에서 외부열교환기(6)로 역류하는 산성가스의 유입을 차단하며, 이 외부 열교환기(6)의 내부에 최종 과열기(28)를 설치하여 450도 이상의 스팀을 생산하면서도 전열관의 부식을 방지하기 위해 HCl과의 직접 접촉을 하지 않도록 하여 부식을 방지함을 특징으로 하는 폐기물과 RPF 연소 전용 순환유동층 보일러.The seal port 5 is non-mechanically controlled without a mechanical device in proportion to the flow rate of the solids for the PRF combustion flow rate control the air, and the particle recirculation passage (21, 22) is separated on both sides, The particle recirculation passage 21 is connected to the particle transfer passage 23 to the combustion furnace 3, and the particle recirculation passage 22 is connected to the external heat exchanger 6 and remains in the seal port 5. Blocks the inflow of acid gas back to the external heat exchanger (6) in the combustor, and installs the final superheater (28) inside the external heat exchanger (6) to produce steam of 450 degrees or more while preventing corrosion of the heat pipe. A circulating fluidized bed boiler dedicated to waste and RPF combustion, characterized by preventing corrosion by avoiding direct contact with HCl to prevent corrosion. 제1항에 있어서, The method of claim 1, 외부 열 교환기(6)는 시일포트(5)에서 연료 이송로(21, 22)가 두 방향으로 연결되며, 연료 이송로(21)와 만나 연료 투입구(31)가 연소로(3)에 연결되도록 함을 특징으로 하는 폐기물과 RPF 연소 전용 순환유동층 보일러.The external heat exchanger 6 is connected to the fuel transport paths 21 and 22 in two directions at the seal port 5, and meets the fuel transport path 21 so that the fuel inlet 31 is connected to the combustion furnace 3. A circulating fluidized bed boiler dedicated to waste and RPF combustion.
KR1020050109232A 2005-11-15 2005-11-15 Circulating fluidized bed boiler for combustion of waste and RPF KR100699519B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
KR1020050109232A KR100699519B1 (en) 2005-11-15 2005-11-15 Circulating fluidized bed boiler for combustion of waste and RPF

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
KR1020050109232A KR100699519B1 (en) 2005-11-15 2005-11-15 Circulating fluidized bed boiler for combustion of waste and RPF

Publications (1)

Publication Number Publication Date
KR100699519B1 true KR100699519B1 (en) 2007-03-23

Family

ID=41564518

Family Applications (1)

Application Number Title Priority Date Filing Date
KR1020050109232A KR100699519B1 (en) 2005-11-15 2005-11-15 Circulating fluidized bed boiler for combustion of waste and RPF

Country Status (1)

Country Link
KR (1) KR100699519B1 (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101093333B1 (en) 2010-08-24 2011-12-14 김문수 Recycling system of waste heat using the fluidized incinerator
CN101900326B (en) * 2009-12-29 2012-07-18 广东兆丰能源技术有限公司 Stokehole pulverized coal recovery type recirculating fluidized bed boiler
KR20180000380A (en) 2016-06-22 2018-01-03 한국에너지기술연구원 Circulating fluidized bed combustion boiler for solid refused fuel with tube corrosion prevent and clinkers reduction fuction
KR20180034763A (en) * 2016-09-27 2018-04-05 한국에너지기술연구원 Apparatus for controlling solid flow in circulating fluidized bed boiler
KR20180073783A (en) 2016-12-22 2018-07-03 한국에너지기술연구원 A Circilation Fluidized Bed Boiler for Overcome Combustion Failure in a Circulating Fluidized Bed Boiler Using Solid Fuel Containing Nonflammable and Chorine Component
CN108361687A (en) * 2018-04-11 2018-08-03 山西沁新能源集团股份有限公司 A kind of boiler dusting ash extracorporal circulatory system guarantee flue gas ultra-clean exhaust system
WO2019168211A1 (en) * 2018-02-27 2019-09-06 한국에너지기술연구원 Flow rate control unit and control method for controlling solid flow between fluidized bed furnace and cyclone, and circulating fluidized bed boiler including flow rate control unit and operating method therefor
KR102381714B1 (en) 2020-10-14 2022-04-05 한국에너지기술연구원 System that burns waste with flexibility in operating capacity

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH10253011A (en) 1997-03-13 1998-09-25 Hitachi Zosen Corp Combustion apparatus
KR19990044099A (en) * 1995-08-21 1999-06-25 아서 이. 퓨니어 쥬니어 A method for reactivating an adsorbent so as to be reusable
JP2000146116A (en) 1998-11-11 2000-05-26 Electric Power Dev Co Ltd Combustion apparatus and corrosion preventing method of heat exchanger tube thereof
KR20030040051A (en) * 2001-11-12 2003-05-22 이시카와지마-하리마 주고교 가부시키가이샤 Circulating fluidized bed boiler
JP2004347145A (en) 2003-05-20 2004-12-09 Ishikawajima Harima Heavy Ind Co Ltd Aluminum deposition preventing method for rpf fired circulation fluidized bed boiler

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR19990044099A (en) * 1995-08-21 1999-06-25 아서 이. 퓨니어 쥬니어 A method for reactivating an adsorbent so as to be reusable
JPH10253011A (en) 1997-03-13 1998-09-25 Hitachi Zosen Corp Combustion apparatus
JP2000146116A (en) 1998-11-11 2000-05-26 Electric Power Dev Co Ltd Combustion apparatus and corrosion preventing method of heat exchanger tube thereof
KR20030040051A (en) * 2001-11-12 2003-05-22 이시카와지마-하리마 주고교 가부시키가이샤 Circulating fluidized bed boiler
JP2004347145A (en) 2003-05-20 2004-12-09 Ishikawajima Harima Heavy Ind Co Ltd Aluminum deposition preventing method for rpf fired circulation fluidized bed boiler

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101900326B (en) * 2009-12-29 2012-07-18 广东兆丰能源技术有限公司 Stokehole pulverized coal recovery type recirculating fluidized bed boiler
KR101093333B1 (en) 2010-08-24 2011-12-14 김문수 Recycling system of waste heat using the fluidized incinerator
KR20180000380A (en) 2016-06-22 2018-01-03 한국에너지기술연구원 Circulating fluidized bed combustion boiler for solid refused fuel with tube corrosion prevent and clinkers reduction fuction
KR20180034763A (en) * 2016-09-27 2018-04-05 한국에너지기술연구원 Apparatus for controlling solid flow in circulating fluidized bed boiler
KR101942247B1 (en) * 2016-09-27 2019-01-28 한국에너지기술연구원 Apparatus for controlling solid flow in circulating fluidized bed boiler
KR20180073783A (en) 2016-12-22 2018-07-03 한국에너지기술연구원 A Circilation Fluidized Bed Boiler for Overcome Combustion Failure in a Circulating Fluidized Bed Boiler Using Solid Fuel Containing Nonflammable and Chorine Component
WO2019168211A1 (en) * 2018-02-27 2019-09-06 한국에너지기술연구원 Flow rate control unit and control method for controlling solid flow between fluidized bed furnace and cyclone, and circulating fluidized bed boiler including flow rate control unit and operating method therefor
CN108361687A (en) * 2018-04-11 2018-08-03 山西沁新能源集团股份有限公司 A kind of boiler dusting ash extracorporal circulatory system guarantee flue gas ultra-clean exhaust system
KR102381714B1 (en) 2020-10-14 2022-04-05 한국에너지기술연구원 System that burns waste with flexibility in operating capacity

Similar Documents

Publication Publication Date Title
KR100699519B1 (en) Circulating fluidized bed boiler for combustion of waste and RPF
Lumley et al. Techno-economic analysis of wastewater sludge gasification: A decentralized urban perspective
KR101805700B1 (en) Combustion improvement method for incinerator in complex facility, and complex facility
EP2933030B1 (en) Waste and sewage treatment system
KR101867160B1 (en) Circulating fluidized bed combustion boiler for solid refused fuel with tube corrosion prevent and clinkers reduction fuction
JP6958489B2 (en) Energy storage and supply equipment by waste incinerator
JP4400467B2 (en) Method and apparatus for burning hydrous waste
KR101142953B1 (en) The trash incinerator and the apparatus for generating power and supplying hot water using thereof
KR101354938B1 (en) Fluidized bed combustor
CN112062435B (en) Oil sludge pyrolysis treatment device and process thereof
KR101309279B1 (en) All fluidize bed that phlogiston device and produce steam resource
JP4241578B2 (en) Method and apparatus for burning hydrous waste
KR101976467B1 (en) A Circilation Fluidized Bed Boiler for Overcome Combustion Failure in a Circulating Fluidized Bed Boiler Using Solid Fuel Containing Nonflammable and Chorine Component
CN103528054B (en) The organic working medium boiler of municipal sludge-water-coal-slurry multifuel combustion
KR101806396B1 (en) Incinerator heat recovery system according to the water-cooled wall
CN203431878U (en) Novel pure-combustion garbage fluidized bed incinerator
CN216431752U (en) Material returning structure for preventing high-temperature corrosion of solid waste furnace
TWI642877B (en) Procede et installation de valorisation energetique de dechets
JP4449704B2 (en) Combustion method and apparatus
JPH0861015A (en) Refuse power generating system
JPH109545A (en) Waste-burning boiler
Highley The development of fluidized bed combustion
CN203052618U (en) Industrial wastewater incineration waste heat boiler
KR20230162438A (en) Circulating fluidized bed boiler using quicklime and method for operating the same
JP2018173061A (en) Power generation system and power generation method

Legal Events

Date Code Title Description
A201 Request for examination
E902 Notification of reason for refusal
E701 Decision to grant or registration of patent right
GRNT Written decision to grant
FPAY Annual fee payment

Payment date: 20130320

Year of fee payment: 7

FPAY Annual fee payment

Payment date: 20140305

Year of fee payment: 8

FPAY Annual fee payment

Payment date: 20150313

Year of fee payment: 9

FPAY Annual fee payment

Payment date: 20160309

Year of fee payment: 10

FPAY Annual fee payment

Payment date: 20170102

Year of fee payment: 11

FPAY Annual fee payment

Payment date: 20180209

Year of fee payment: 12

FPAY Annual fee payment

Payment date: 20181211

Year of fee payment: 13

FPAY Annual fee payment

Payment date: 20191210

Year of fee payment: 14