CN107654276A - The processing system of ship double fuel or natural gas engine escape methane - Google Patents
The processing system of ship double fuel or natural gas engine escape methane Download PDFInfo
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- CN107654276A CN107654276A CN201711101597.9A CN201711101597A CN107654276A CN 107654276 A CN107654276 A CN 107654276A CN 201711101597 A CN201711101597 A CN 201711101597A CN 107654276 A CN107654276 A CN 107654276A
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- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 title claims abstract description 160
- 239000003345 natural gas Substances 0.000 title claims abstract description 22
- 239000002737 fuel gas Substances 0.000 title claims abstract description 21
- 230000003647 oxidation Effects 0.000 claims abstract description 61
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 61
- 239000007789 gas Substances 0.000 claims abstract description 54
- 239000003054 catalyst Substances 0.000 claims abstract description 42
- 230000003197 catalytic effect Effects 0.000 claims abstract description 12
- 238000006555 catalytic reaction Methods 0.000 claims abstract description 8
- 230000001590 oxidative effect Effects 0.000 claims 1
- 238000003912 environmental pollution Methods 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 20
- 239000000446 fuel Substances 0.000 description 15
- 229930195733 hydrocarbon Natural products 0.000 description 13
- 150000002430 hydrocarbons Chemical class 0.000 description 13
- 239000003344 environmental pollutant Substances 0.000 description 12
- 231100000719 pollutant Toxicity 0.000 description 9
- 239000002828 fuel tank Substances 0.000 description 5
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 239000005431 greenhouse gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 238000013016 damping Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000010687 lubricating oil Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- WSFSSNUMVMOOMR-NJFSPNSNSA-N methanone Chemical compound O=[14CH2] WSFSSNUMVMOOMR-NJFSPNSNSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical class S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N3/00—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust
- F01N3/08—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous
- F01N3/10—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust
- F01N3/24—Exhaust or silencing apparatus having means for purifying, rendering innocuous, or otherwise treating exhaust for rendering innocuous by thermal or catalytic conversion of noxious components of exhaust characterised by constructional aspects of converting apparatus
- F01N3/36—Arrangements for supply of additional fuel
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/46—Removing components of defined structure
- B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N9/00—Electrical control of exhaust gas treating apparatus
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B43/00—Engines characterised by operating on gaseous fuels; Plants including such engines
- F02B43/10—Engines or plants characterised by use of other specific gases, e.g. acetylene, oxyhydrogen
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B69/00—Internal-combustion engines convertible into other combustion-engine type, not provided for in F02B11/00; Internal-combustion engines of different types characterised by constructions facilitating use of same main engine-parts in different types
- F02B69/02—Internal-combustion engines convertible into other combustion-engine type, not provided for in F02B11/00; Internal-combustion engines of different types characterised by constructions facilitating use of same main engine-parts in different types for different fuel types, other than engines indifferent to fuel consumed, e.g. convertible from light to heavy fuel
- F02B69/04—Internal-combustion engines convertible into other combustion-engine type, not provided for in F02B11/00; Internal-combustion engines of different types characterised by constructions facilitating use of same main engine-parts in different types for different fuel types, other than engines indifferent to fuel consumed, e.g. convertible from light to heavy fuel for gaseous and non-gaseous fuels
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2570/00—Exhaust treating apparatus eliminating, absorbing or adsorbing specific elements or compounds
- F01N2570/12—Hydrocarbons
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F01—MACHINES OR ENGINES IN GENERAL; ENGINE PLANTS IN GENERAL; STEAM ENGINES
- F01N—GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR MACHINES OR ENGINES IN GENERAL; GAS-FLOW SILENCERS OR EXHAUST APPARATUS FOR INTERNAL COMBUSTION ENGINES
- F01N2590/00—Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines
- F01N2590/02—Exhaust or silencing apparatus adapted to particular use, e.g. for military applications, airplanes, submarines for marine vessels or naval applications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02B—INTERNAL-COMBUSTION PISTON ENGINES; COMBUSTION ENGINES IN GENERAL
- F02B43/00—Engines characterised by operating on gaseous fuels; Plants including such engines
- F02B43/10—Engines or plants characterised by use of other specific gases, e.g. acetylene, oxyhydrogen
- F02B2043/103—Natural gas, e.g. methane or LNG used as a fuel
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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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/30—Use of alternative fuels, e.g. biofuels
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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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/40—Engine management systems
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- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
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- Exhaust Gas After Treatment (AREA)
Abstract
本发明提供的是一种船舶双燃料或天然气发动机逃逸甲烷的处理系统。包括连接在发动机排气管道后的氧化催化器,还包括补燃器,补燃器通过单独的补燃器油泵与油箱相连,补燃器的出口并入发动机排气管道加热排气管道中的来自发动机的含甲烷尾气,使尾气温度达到甲烷氧化催化所需温度。本发明通过加装补燃器以提高船舶双燃料/天然气发动机尾气的温度,进而利用氧化催化装置去除来自双燃料/天然气发动机的逃逸甲烷,减少了环境污染。
The invention provides a treatment system for escaped methane from a ship's dual-fuel or natural gas engine. It includes an oxidation catalyst connected behind the exhaust pipe of the engine, and a post-burner, which is connected to the oil tank through a separate post-burner oil pump, and the outlet of the post-burner is integrated into the engine exhaust pipe to heat the exhaust gas in the exhaust pipe. The methane-containing exhaust gas from the engine makes the exhaust gas temperature reach the temperature required for methane oxidation catalysis. The invention increases the temperature of the tail gas of the ship's dual-fuel/natural gas engine by adding a supplementary burner, and then uses an oxidation catalytic device to remove escaped methane from the dual-fuel/natural gas engine, thereby reducing environmental pollution.
Description
技术领域technical field
本发明涉及的是一种发动机逃逸甲烷的排放后处理系统,具体地说是一种船舶双燃料发动机/天然气发动机逃逸甲烷的排放后处理系统。The invention relates to an exhaust post-treatment system for escaped methane from an engine, in particular to an exhaust post-treatment system for escaped methane from a ship's dual-fuel engine/natural gas engine.
背景技术Background technique
船舶双燃料/天然气发动机以其燃料(CH4)来源多,燃料成本低,与传统船舶低速发动机相比,NOx排放降低20%以上,几乎没有硫氧化物和颗粒物排放,正在江海和远洋船舶上获得越来越多的应用。但双燃料/天然气发动机的HC排放,尤其是基于Otto循环的双燃料/天然气发动机的甲烷(CH4)排放较多,对环境产生了严重的污染。Marine dual-fuel/natural gas engines have many sources of fuel (CH 4 ) and low fuel costs. Compared with traditional low-speed marine engines, NOx emissions are reduced by more than 20%, and there are almost no sulfur oxides and particulate matter emissions. They are being used on river, sea and ocean-going ships. Get more and more applications. However, HC emissions from dual-fuel/natural gas engines, especially methane (CH 4 ) emissions from dual-fuel/natural gas engines based on the Otto cycle are relatively large, causing serious pollution to the environment.
目前IMO及世界各国的环保法规越来越严格,对船舶发动机尾气排放的控制要求也越来越严格,如何采取有效手段降低发动机污染物的排放成为发动机排放技术研究领域的重要课题。碳氢化合物(HC)是双燃料/天然气发动机的主要排放物,主要包括甲烷及其衍生物(甲醛CH2O和甲醇CH3OH)等。At present, the environmental protection regulations of IMO and other countries in the world are becoming more and more stringent, and the requirements for the control of ship engine exhaust emissions are also becoming more and more stringent. How to take effective measures to reduce the emission of engine pollutants has become an important topic in the field of engine emission technology research. Hydrocarbons (HC) are the main emissions of dual-fuel/natural gas engines, mainly including methane and its derivatives (formaldehyde CH 2 O and methanol CH 3 OH).
船舶双燃料/天然气发动机排放的碳氢化合物包括未燃和未完全燃烧的燃料、润滑油及其裂解产物和部分氧化物,如甲烷、甲醛、苯、醛、酮及有关衍生物等200多种成分。为了减少碳氢化合物的排放,在发动机排气后处理系统中安装DOC(Diesel OxidationCatalyst,氧化催化器)是目前主要的技术手段。氧化催化器由壳体、减振层、载体及催化剂四部分构成,随着尾气通过氧化催化器,其中的CO、碳氢化合物等污染物(除甲烷外)会被氧化,从而减少污染物排放。Hydrocarbons emitted by marine dual-fuel/natural gas engines include unburned and incompletely burned fuels, lubricating oils and their cracking products and partial oxides, such as more than 200 kinds of methane, formaldehyde, benzene, aldehydes, ketones and related derivatives Element. In order to reduce the emission of hydrocarbons, installing DOC (Diesel Oxidation Catalyst, oxidation catalyst) in the engine exhaust aftertreatment system is the main technical means at present. The oxidation catalyst is composed of four parts: housing, vibration damping layer, carrier and catalyst. As the exhaust gas passes through the oxidation catalyst, pollutants such as CO and hydrocarbons (except methane) will be oxidized, thereby reducing pollutant emissions .
碳氢化合物中的甲烷是热势很高的温室效应气体,其温暖化潜势要比二氧化碳大21倍。甲烷是一种高度稳定的化合物,需要很高的活化能来破坏碳氢键和氧化甲烷分子。有效地氧化催化甲烷需要尾气温度高于600℃。由于从双燃料/天然气发动机排出的尾气温度较低,尾气后处理系统中的氧化催化器难以将其中的甲烷这一温室效应成分去除。Methane among hydrocarbons is a greenhouse gas with a high thermal potential, and its warming potential is 21 times greater than that of carbon dioxide. Methane is a highly stable compound that requires high activation energy to break carbon-hydrogen bonds and oxidize methane molecules. Effective oxidation of catalytic methane requires tail gas temperatures above 600°C. Oxidation catalysts in exhaust aftertreatment systems have difficulty removing methane, a greenhouse effect component, from exhaust gases from dual-fuel/natural gas engines due to their low temperatures.
现有技术中,关于发动机尾气的氧化催化技术主要有:In the prior art, the oxidation catalytic technologies for engine exhaust mainly include:
1、申请号为201020620945.0的专利文件中公开的“柴油发动机氧化催化器”,设计了一种柴油发动机氧化催化器,采用蚌壳式封装为一体,使用价格较低的钯,降低了生产成本。但该装置只适用于车用柴油发动机,且氧化催化效率不够高,也无法去除船舶双燃料/天然气发动机尾气成分中的甲烷。1. The "diesel engine oxidation catalyst" disclosed in the patent document with application number 201020620945.0 is a design of a diesel engine oxidation catalyst, which is packaged in a clam shell and uses lower-priced palladium to reduce production costs. However, this device is only suitable for vehicle diesel engines, and the oxidation catalytic efficiency is not high enough, nor can it remove methane in the exhaust components of marine dual-fuel/natural gas engines.
2、申请号为201180074031.6的专利文件中公开的“柴油机氧化催化器和处理发动机排气的方法”,设计了一种柴油机氧化催化器,该装置对氧化催化器的入口端和出口端通道进行了改进,有利于改善氧化催化器易受烟尘和碳氢化合物颗粒的堵塞问题。但该装置针对柴油机设计,且氧化催化温度较低,不能够处理船舶双燃料/天然气发动机尾气成分中的甲烷。2. The "Diesel Oxidation Catalyst and Method for Treating Engine Exhaust" disclosed in the patent document with application number 201180074031.6, designed a diesel oxidation catalyst, the device has carried out the inlet port and outlet channel of the oxidation catalyst Improvement, which is beneficial to improve the problem that the oxidation catalyst is susceptible to clogging by soot and hydrocarbon particles. However, the device is designed for diesel engines and has a low oxidation and catalytic temperature, so it cannot handle methane in the exhaust components of marine dual-fuel/natural gas engines.
发明内容Contents of the invention
本发明的目的在于提供一种能够去除包括普通氧化催化器不能氧化的甲烷在内的多种环境污染物,减少船舶尾气污染物和温室效应气体排放的船舶双燃料或天然气发动机逃逸甲烷的处理系统。The object of the present invention is to provide a kind of treatment system that can remove multiple environmental pollutants including methane that cannot be oxidized by ordinary oxidation catalytic converters, reduce ship exhaust pollutants and greenhouse effect gas emissions, and escape methane from ship dual-fuel or natural gas engines .
本发明的目的是这样实现的:The purpose of the present invention is achieved like this:
包括连接在发动机排气管道后的氧化催化器,还包括补燃器,补燃器通过单独的补燃器油泵与油箱相连,补燃器的出口并入发动机排气管道加热排气管道中的来自发动机的含甲烷尾气,使尾气温度达到甲烷氧化催化所需温度。It includes the oxidation catalyst connected behind the exhaust pipe of the engine, and also includes the afterburner. The afterburner is connected to the oil tank through a separate afterburner oil pump. The outlet of the afterburner is integrated into the engine exhaust pipe to heat the exhaust pipe. The methane-containing exhaust gas from the engine makes the exhaust gas temperature reach the temperature required for methane oxidation catalysis.
本发明还可以包括:The present invention may also include:
还包括温度传感器和电控装置,温度传感器安装在补燃器的出口并入之后的发动机排气管道上,温度传感器监测氧化催化器前的尾气温度输入电控装置,电控装置控制补燃器油泵和补燃器。It also includes a temperature sensor and an electronic control device. The temperature sensor is installed on the exhaust pipe of the engine after the outlet of the afterburner is incorporated. The temperature sensor monitors the exhaust gas temperature before the oxidation catalyst and inputs it into the electronic control device, and the electronic control device controls the afterburner. Oil pump and afterburner.
本发明提供了一种能够去除包括甲烷在内的多种环境污染物的船舶双燃料/天然气发动机的尾气后处理氧化催化装置。该系统由氧化催化装置和补燃器相结合,能够将发动机尾气温度提高到满足甲烷氧化催化的温度,去除包括普通氧化催化器不能氧化的甲烷在内的多种环境污染物,减少船舶尾气污染物和温室效应气体的排放。The invention provides an oxidation catalytic device for post-treatment exhaust gas of a marine dual-fuel/natural gas engine capable of removing various environmental pollutants including methane. The system is composed of an oxidation catalytic device and an afterburner, which can increase the temperature of the engine exhaust gas to the temperature required for methane oxidation and catalysis, remove various environmental pollutants including methane that cannot be oxidized by ordinary oxidation catalysts, and reduce ship exhaust pollution. emissions of pollutants and greenhouse gases.
本发明的技术方案包括氧化催化器、补燃器、温度传感器、电控装置、泵及管路。补燃器通过单独的补燃器油泵与油箱相连,补燃器和输油泵与电控装置连接。氧化催化器安装在发动机排气管道中,尾气从发动机进入排气管道,当需要处理船舶双燃料/天然气尾气中的甲烷时,补燃器开始工作,燃料箱中的燃料经由输油泵向补燃器供油,补燃器产生的高温排气并入发动机排气管道中,加热排气管道中的来自发动机的含甲烷尾气,温度传感器监测氧化催化器前的尾气温度,通过电控装置选择启停补燃器。该系统通过加装补燃器提高尾气氧化催化的温度,使其达到甲烷氧化催化所需温度,从而达到去除尾气中逃逸甲烷的目的。The technical solution of the invention includes an oxidation catalyst, an afterburner, a temperature sensor, an electric control device, a pump and pipelines. The afterburner is connected with the fuel tank through a separate afterburner oil pump, and the afterburner and the oil delivery pump are connected with the electric control device. The oxidation catalyst is installed in the exhaust pipe of the engine, and the exhaust gas enters the exhaust pipe from the engine. When it is necessary to deal with the methane in the dual fuel/natural gas exhaust gas of the ship, the afterburner starts to work, and the fuel in the fuel tank is sent to the afterburner through the oil transfer pump. The high-temperature exhaust gas produced by the afterburner is incorporated into the engine exhaust pipe to heat the methane-containing exhaust gas from the engine in the exhaust pipe. The temperature sensor monitors the exhaust gas temperature in front of the oxidation catalyst and selects the start Stop the burner. The system increases the temperature of tail gas oxidation and catalysis by adding an afterburner to make it reach the temperature required for methane oxidation and catalysis, so as to achieve the purpose of removing escaped methane from tail gas.
本发明的技术方案的主要特点体现在:The main features of the technical solution of the present invention are reflected in:
1、利用高温排气,提高船舶双燃料/天然气发动机尾气的温度,使之达到氧化催化器能够去除甲烷的温度,以在氧化催化器中氧化掉发动机尾气中的逃逸甲烷。1. Use high-temperature exhaust to increase the temperature of the exhaust gas of the ship's dual-fuel/natural gas engine so that it reaches the temperature at which the oxidation catalyst can remove methane, so that the escaped methane in the engine exhaust gas can be oxidized in the oxidation catalyst.
2、采用补燃器和氧化催化器相结合的方法。2. The method of combining the afterburner and the oxidation catalyst is adopted.
3、对尾气的温度进行控制,以保证氧化催化器中的尾气温度在能够氧化催化甲烷的适宜范围内。3. Control the temperature of the exhaust gas to ensure that the temperature of the exhaust gas in the oxidation catalyst is within a suitable range for oxidation and catalytic methane.
4、通过补燃器的尾气温度控制为600℃~750℃。4. The temperature of the exhaust gas passing through the afterburner is controlled to be 600°C to 750°C.
5、补燃器的进口端依次连接补燃器油泵和油箱,发动机排气管道上设有氧化催化器,温度传感器布置在氧化催化器前的排气管道上,电控装置的输入端连接温度传感器,输出端连接补燃器和补燃器油泵。补燃器产生的高温排气通过补燃器排气管道汇入发动机排气管道,和发动机产生的含甲烷尾气一并流入氧化催化器。5. The inlet end of the afterburner is connected to the oil pump of the afterburner and the fuel tank in turn. An oxidation catalyst is installed on the exhaust pipe of the engine. The temperature sensor is arranged on the exhaust pipe in front of the oxidation catalyst. The input end of the electronic control device is connected to the temperature The output end of the sensor is connected to the afterburner and the oil pump of the afterburner. The high-temperature exhaust gas produced by the afterburner flows into the engine exhaust pipe through the exhaust pipe of the afterburner, and flows into the oxidation catalyst together with the methane-containing exhaust gas produced by the engine.
6、来源于船舶双燃料/天然气发动机的含甲烷尾气通过排气管道进入氧化催化器,温度传感器测量氧化催化器前的尾气温度,将温度信号输入电控装置中,如果温度低于600℃(甲烷氧化催化反应温度),电控装置输出信号,使补燃器油泵喷油,补燃器点火运行,补燃器产生高温排气汇入发动机排气管道中,加热排气管道中的尾气。如果温度传感器输入到电控装置的温度信号高于750℃,则电控装置输出信号使补燃器油泵和补燃器停止运行,从而使得流经氧化催化器的尾气温度保持在能够氧化催化甲烷的适宜范围内,从而达到去除甲烷的目的,同时也能够氧化CO、碳氢化合物(除甲烷外)及其他污染物。6. The methane-containing tail gas from the ship's dual-fuel/natural gas engine enters the oxidation catalyst through the exhaust pipe. The temperature sensor measures the temperature of the exhaust gas in front of the oxidation catalyst, and inputs the temperature signal into the electronic control device. If the temperature is lower than 600°C ( methane oxidation catalytic reaction temperature), the output signal of the electronic control device makes the afterburner oil pump inject oil, the afterburner ignites and runs, and the afterburner generates high-temperature exhaust gas that flows into the engine exhaust pipe to heat the exhaust gas in the exhaust pipe. If the temperature signal input by the temperature sensor to the electronic control device is higher than 750°C, the output signal of the electronic control device will stop the operation of the afterburner oil pump and the afterburner, so that the temperature of the exhaust gas flowing through the oxidation catalyst can be kept at a temperature that can oxidize and catalyze methane In the appropriate range, so as to achieve the purpose of removing methane, but also can oxidize CO, hydrocarbons (except methane) and other pollutants.
7、当船舶双燃料发动机工作在燃油模式或发动机运行工况不需要去除甲烷时,电控装置控制补燃器油泵和补燃器关闭,不产生高温排气,氧化催化器中只有从发动机产生的尾气流过,此时可以完成氧化CO、碳氢化合物(除甲烷外)及其他污染物,能够有效节约能耗,提高经济性。7. When the ship's dual-fuel engine works in fuel mode or the engine operating condition does not need to remove methane, the electronic control device controls the afterburner oil pump and the afterburner to shut down, no high-temperature exhaust gas is produced, and only the engine generates At this time, CO, hydrocarbons (except methane) and other pollutants can be oxidized, which can effectively save energy consumption and improve economy.
8、根据船舶双燃料发动机的运行模式或发动机的运行工况来主动选择是否需要处理尾气中的甲烷。8. According to the operating mode of the ship's dual-fuel engine or the operating conditions of the engine, it is actively selected whether to deal with the methane in the tail gas.
本发明与现有技术相比的优势在于:The advantage of the present invention compared with prior art is:
(1)氧化催化器与补燃器联合,提高了尾气氧化催化反应的温度,能够去除普通氧化催化器不能去除的甲烷,减少了发动机尾气HC排放和温室效应气体排放。(1) The combination of the oxidation catalyst and the afterburner increases the temperature of the exhaust gas oxidation catalytic reaction, can remove the methane that cannot be removed by the ordinary oxidation catalyst, and reduces the emission of engine exhaust HC and greenhouse gas.
(2)补燃器独立于发动机排气管道之外,对发动机燃烧性能影响很小。(2) The afterburner is independent from the engine exhaust pipe, and has little influence on the combustion performance of the engine.
(3)当船舶双燃料发动机运行在燃油模式或运行工况不需要去除甲烷时,可以通过电控装置停止运行补燃器,使尾气在较低的温度下氧化催化,能有效减少能耗,提高经济性。(3) When the marine dual-fuel engine is running in the fuel mode or the operating condition does not need to remove methane, the afterburner can be stopped through the electronic control device, so that the exhaust gas can be oxidized and catalyzed at a lower temperature, which can effectively reduce energy consumption. Improve economy.
附图说明Description of drawings
图1为本发明的示意图。Figure 1 is a schematic diagram of the present invention.
具体实施方式Detailed ways
下面举例对本发明做更详细的描述。The following examples describe the present invention in more detail.
结合图1,本发明主要包括氧化催化器8、补燃器5、补燃器油泵4、电控装置6、温度传感器7及附属管路和控制线路。补燃器5的进口端依次连接补燃器油泵4和油箱1,发动机2通过油路与发动机燃油泵3和油箱1相连(发动机燃油模式或引燃气体燃料时用),发动机排气管道上设有氧化催化器8,温度传感器7布置在氧化催化器8前的排气管道上,电控装置6的输入端连接温度传感器7,输出端连接补燃器5和补燃器油泵4。补燃器5产生的高温排气通过补燃器排气管道汇入发动机排气管道,和发动机2产生的含甲烷尾气一并流入氧化催化器8。Referring to Fig. 1, the present invention mainly includes an oxidation catalyst 8, an afterburner 5, an afterburner oil pump 4, an electronic control device 6, a temperature sensor 7, and auxiliary pipelines and control lines. The inlet end of the afterburner 5 is connected to the afterburner oil pump 4 and the fuel tank 1 in turn, the engine 2 is connected to the engine fuel pump 3 and the fuel tank 1 through the oil circuit (for engine fuel mode or pilot gas fuel), and the engine exhaust pipe An oxidation catalyst 8 is provided, and a temperature sensor 7 is arranged on the exhaust pipe in front of the oxidation catalyst 8. The input end of the electronic control device 6 is connected to the temperature sensor 7, and the output end is connected to the afterburner 5 and the afterburner oil pump 4. The high-temperature exhaust gas generated by the afterburner 5 flows into the engine exhaust pipe through the afterburner exhaust pipe, and flows into the oxidation catalyst 8 together with the methane-containing tail gas generated by the engine 2 .
本装置氧化催化甲烷的功能是这样实现的:来源于船舶双燃料/天然气发动机2的含甲烷尾气通过排气管道进入氧化催化器8,温度传感器7测量氧化催化器8前的尾气温度,将温度信号输入电控装置6中,如果温度低于600℃,电控装置6输出信号,使补燃器油泵4喷油,补燃器5点火运行,补燃器5产生高温的排气汇入发动机排气管道中,加热排气管道中的含甲烷尾气。如果温度传感器7输入到电控装置6的温度信号高于750℃,则电控装置6输出信号使补燃器油泵4和补燃器5停止运行,从而使得流经氧化催化器8的尾气温度保持在能够氧化催化甲烷的适宜范围内,从而达到去除甲烷的目的,同时也能够氧化CO、碳氢化合物(除甲烷外)及其他污染物。The function of this device to oxidize and catalyze methane is realized in this way: the methane-containing tail gas from the ship's dual-fuel/natural gas engine 2 enters the oxidation catalyst 8 through the exhaust pipe, and the temperature sensor 7 measures the temperature of the tail gas before the oxidation catalyst 8, and the temperature The signal is input into the electronic control device 6. If the temperature is lower than 600°C, the electronic control device 6 outputs a signal to make the afterburner oil pump 4 inject oil, the afterburner 5 ignites and run, and the afterburner 5 generates high-temperature exhaust gas to flow into the engine In the exhaust line, the methane-containing tail gas in the exhaust line is heated. If the temperature signal input by the temperature sensor 7 to the electronic control device 6 is higher than 750°C, the electronic control device 6 outputs a signal to stop the operation of the afterburner oil pump 4 and the afterburner 5, so that the temperature of the exhaust gas flowing through the oxidation catalyst 8 Keep within the appropriate range for oxidation and catalytic methane, so as to achieve the purpose of methane removal, and also be able to oxidize CO, hydrocarbons (except methane) and other pollutants.
当船舶双燃料发动机运行在燃油模式或发动机运行工况不需要处理甲烷时,电控装置6控制补燃器油泵4和补燃器5关闭,不产生高温排气,氧化催化器8中只有从发动机2产生的尾气流过,此时可以完成氧化CO、碳氢化合物(除甲烷外)及其他污染物,能够有效减少能耗,提高经济性。When the ship's dual-fuel engine is running in fuel mode or the engine operating condition does not need to deal with methane, the electronic control device 6 controls the afterburner oil pump 4 and the afterburner 5 to close, no high-temperature exhaust gas is generated, and only the secondary burner in the oxidation catalyst 8 The exhaust gas produced by the engine 2 flows through, and at this time, the oxidation of CO, hydrocarbons (except methane) and other pollutants can be completed, which can effectively reduce energy consumption and improve economy.
虽然本faming中已经结合实施例对本发明进行了描述,但应该理解的是,本发明不局限于所公开的实施方式,而是在如所附权利要求中限定的一样涵盖其特征的各种组合或者修改已经包含在本发明的范围内的一些其他应用。While the invention has been described in connection with the examples in this faming, it is to be understood that the invention is not limited to the disclosed embodiments but encompasses various combinations of features thereof as defined in the appended claims Or modify some other applications already included within the scope of the present invention.
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