CN109373336B - Natural gas combines fuel exhaust gas and cleans fusion agent high-pressure common rail premixing combustion apparatus - Google Patents

Natural gas combines fuel exhaust gas and cleans fusion agent high-pressure common rail premixing combustion apparatus Download PDF

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Publication number
CN109373336B
CN109373336B CN201811181061.7A CN201811181061A CN109373336B CN 109373336 B CN109373336 B CN 109373336B CN 201811181061 A CN201811181061 A CN 201811181061A CN 109373336 B CN109373336 B CN 109373336B
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exhaust gas
fuel exhaust
fusion agent
parts
natural gas
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CN201811181061.7A
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CN109373336A (en
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陶哲瀚
孙峤楠
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Zhejiang Youchi Energy Technology Co Ltd
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Zhejiang Youchi Energy Technology Co Ltd
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G7/00Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
    • F23G7/06Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
    • F23G7/061Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating
    • F23G7/065Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases with supplementary heating using gaseous or liquid fuel
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L3/00Gaseous fuels; Natural gas; Synthetic natural gas obtained by processes not covered by subclass C10G, C10K; Liquefied petroleum gas
    • C10L3/003Additives for gaseous fuels
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/02Premix gas burners, i.e. in which gaseous fuel is mixed with combustion air upstream of the combustion zone
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23DBURNERS
    • F23D14/00Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
    • F23D14/46Details, e.g. noise reduction means
    • F23D14/62Mixing devices; Mixing tubes
    • F23D14/64Mixing devices; Mixing tubes with injectors
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/04Organic compounds
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
    • C10L2200/00Components of fuel compositions
    • C10L2200/04Organic compounds
    • C10L2200/0407Specifically defined hydrocarbon fractions as obtained from, e.g. a distillation column
    • C10L2200/0453Petroleum or natural waxes, e.g. paraffin waxes, asphaltenes

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The invention discloses a kind of natural gas joint fuel exhaust gas to clean fusion agent high-pressure common rail premixing combustion apparatus, comprising: natural gas motor regulated valve, input terminal are connected to high-pressure natural gas gas source;Fuel exhaust gas cleans fusion agent motor regulated valve, and input terminal cleans fusion agent storage tank through hydraulic pump connection fuel exhaust gas;Mixing chamber is double-layer structure, the output end of the input port connection natural gas motor regulated valve of internal layer, the delivery outlet of the input port connection fuel exhaust gas cleaning fusion agent motor regulated valve of outer layer;Mixing tube, input port are connected to the delivery outlet of mixing chamber internal layer and the delivery outlet of outer layer;Common rail pipe, input port are connected to the delivery outlet of mixing tube;Burner, is provided with gas-liquid mixed pipe and combustion tube, the delivery outlet of the input terminal connection common rail pipe of gas-liquid mixed pipe, and the input terminal of combustion tube is connected to air pump through air motor regulated valve;The present invention has simple structure, at low cost, energy conservation and environmental protection, the beneficial effect for zero-emission of burning.

Description

Natural gas combines fuel exhaust gas and cleans fusion agent high-pressure common rail premixing combustion apparatus
Technical field
The present invention relates to a kind of natural gas joint fuel exhaust gas to clean fusion agent high-pressure common rail premixing combustion apparatus.
Background technique
Recently, country, which proposes, " carries out Industrial Boiler kiln, heavy-duty diesel oil engineering truck, farm machinery, ship shipping oil Discharge beyond standards special administration ", stage by stage complete rebuilding and improving task, in by the end of October, 2018 before, complete 10 steam the above combustion gas of ton The transformation of boiler low nitrogen burning;The 1-10 that completes preceding in by the end of October, 2019 steams ton (steaming ton and 10 steaming tons containing 1) gas fired-boiler low nitrogen burning Transformation;To the year two thousand twenty by the end of June before, existing non-electrical gas-steam boiler, hot-water boiler, layer burner and spreader stoker boiler are fully completed low Nitrogen combustion retrofit;Flue dust, sulfur dioxide and nitrogen oxides reach 5mg/m3,10mg/m3,30mg/m3, and it is synchronous to create gas fired-boiler Installation low nitrogen combustion apparatus simultaneously reaches discharge standard requirement;20 steamings ton/hour and the above gas fired-boiler will install the source of atmospheric pollution Automatic monitor and control facility, and network with environmental protection administration, while dcs (DCS system) being installed;20 steamings ton/hour or less Gas fired-boiler will install nitrogen oxides exhaust analyzer.
In everybody impression, natural gas is a kind of clean energy resource, why can still generate NOX pollutant, this is because Gas fired-boiler combustion of natural gas temperature is more than that will start to generate a large amount of nitrogen oxides after 1000 DEG C.
Natural gas main component is alkane, and wherein methane accounts for the overwhelming majority, while also containing micro nitrogen impurity;Natural gas Need air in combustion, and in air 80 parts be nitrogen, under room temperature, nitrogen is a kind of very stable gas, but in height Nitrogen oxides will be generated under the conditions of temperature, nitrous oxides concentration affects PM2.5, and especially Heating Season energy consumption and winter is spread The unfavorable double factor superposition of condition, influences whether the generation of nitrogen oxides.
According to calculating, the amount of nitrogen oxides that 1 ton of combustion of natural gas generates is 6.35 kilograms, and natural gas itself does not generate nitrogen oxidation Object, only ignition temperature is very high, and high temperature produces nitrogen oxides, if it is possible to by burning point temperature control at 800 degree hereinafter, energy Discharge amount of exhaust gas is enough greatly lowered, but the efficiency that burning utilizes also just reduces, this generates contradictions.
In fact, either coal-fired, combustion gas or fuel oil, can all discharge nitrogen oxides, but the weight as Ozone in Atmosphere Precursor is wanted, the increase of nitrous oxides concentration will cause certain secondary pollution, but these can control, nitrogen oxides one It is directly a class of pollutant of China's priority control.
Summary of the invention
The present invention is according to the above deficiency, provide a kind of natural gas joint fuel exhaust gas cleaning fusion agent high-pressure common rail premix Burner can substantially eliminate the generation of oxynitrides, be really achieved burning zero-emission target.
The technical scheme is that
A kind of natural gas joint fuel exhaust gas cleaning fusion agent high-pressure common rail premixing combustion apparatus, characterized in that include:
Natural gas motor regulated valve, input terminal are connected to high-pressure natural gas gas source;
Fuel exhaust gas cleans fusion agent motor regulated valve, and input terminal cleans fusion agent through hydraulic pump connection fuel exhaust gas Storage tank;
Mixing chamber, be double-layer structure, internal layer input port connection natural gas motor regulated valve output end, outer layer it is defeated Entrance is connected to the delivery outlet of fuel exhaust gas cleaning fusion agent motor regulated valve;
Mixing tube, input port are connected to the delivery outlet of mixing chamber internal layer and the delivery outlet of outer layer;
Common rail pipe, input port are connected to the delivery outlet of mixing tube;
Burner, is provided with multiple, is provided with gas-liquid mixed pipe and combustion tube, the output end setting of gas-liquid mixed pipe In the combustion chamber of burner, the delivery outlet of the input terminal connection common rail pipe of gas-liquid mixed pipe, the output end setting of combustion tube In the combustion chamber of burner, the input terminal of combustion tube is connected to air pump through air motor regulated valve;
Controller, electrical connection natural gas motor regulated valve, fuel exhaust gas cleaning fusion agent motor regulated valve and air Motor regulated valve;
Fuel exhaust gas cleans fusion agent and natural gas after mixing chamber is atomized, and is output to common rail pipe through mixing tube, then with sky Burner burning output low pollution thermal energy is input to after gas mixing.
The ratio of each propellant composition can be obtained by controlling each valve by controller, to obtain the heat of low pollution Energy.
Preferably, the mixing chamber is Venturi tube, the nozzle of mixing chamber internal layer is fine taper, the output of mixing chamber outer layer Mouth is big taper.
Venturi-tube action will form gas-liquid cavitation effect, this cavitation effect at the natural gas nozzle mouth of high-speed jet It should be a kind of new technique based on cavitation phenomenon, be extremely complex physics and chemical effect, local gas-liquid phase transition process, phase It is similar to ultrasonic cavitation principle, abrupt release goes out huge energy, forms local high temperature and pressure and strong shock wave and micro- penetrates Stream can produce free radical and cause chain reaction.
Preferably, the mixing tube is taper.
The fuel exhaust gas cleaning fusion agent is made from the following raw materials in parts by weight: 3.5 parts of the tert-butyl alcohol, 75 parts of methanol, first 17 parts of phenylene diisocyanate, 1.5 parts of oleic acid, 2.5 parts of dimethoxy-ethane, 1.5 parts of atoleine, 1.5 parts of naproanilide.
Method acquisition is prepared by the following procedure in the fuel exhaust gas cleaning fusion agent:
3.5 parts of the tert-butyl alcohol is added 17 parts of toluene di-isocyanate(TDI)s and is sufficiently stirred by S1;
S2 adds after 1.5 parts of naproanilide stirrings sufficiently time of repose 15-25 minutes;
1.5 parts of oleic acid, 2.5 parts of dimethoxy-ethanes, 1.5 parts of atoleines are sequentially added stirring 10-20 minutes by S3;
The above deployed component is added in 75 parts of methanol components and is stirred 25-35 minutes by S4, still aging 1.5-2.5 hour is made fuel exhaust gas and cleans fusion agent.
The present invention has simple structure, at low cost, energy conservation and environmental protection, the beneficial effect for zero-emission of burning.
Detailed description of the invention
Fig. 1 is overall structure diagram of the invention.
Specific embodiment
Now in conjunction with attached drawing, the present invention is further illustrated:
As shown, a kind of natural gas joint fuel exhaust gas cleans fusion agent high-pressure common rail premixing combustion apparatus, feature It is, comprising:
Natural gas motor regulated valve 1, input terminal are connected to high-pressure natural gas gas source;
Fuel exhaust gas cleans fusion agent motor regulated valve 3, and input terminal is through hydraulic pump connection fuel exhaust gas cleaning fusion Agent storage tank;
Mixing chamber 2 is double-layer structure, and the input port of internal layer is connected to the output end of natural gas motor regulated valve 1, outer layer Input port is connected to the delivery outlet of fuel exhaust gas cleaning fusion agent motor regulated valve 3;
Mixing tube 4, input port are connected to the delivery outlet of 2 internal layer of mixing chamber and the delivery outlet of outer layer;
Common rail pipe 5, input port are connected to the delivery outlet of mixing tube 4;
Burner 9, is provided with multiple, is provided with gas-liquid mixed pipe 6 and combustion tube 8, the output end of gas-liquid mixed pipe 6 Be arranged in the combustion chamber of burner 9, the delivery outlet of the input terminal of gas-liquid mixed pipe 6 connection common rail pipe 5, combustion tube 8 it is defeated Outlet is arranged in the combustion chamber of burner 9, and the input terminal of combustion tube 8 is connected to air pump 7 through air motor regulated valve;
Controller, electrical connection natural gas motor regulated valve 1, fuel exhaust gas cleaning fusion agent motor regulated valve 3 and sky Gas motor regulated valve;
Fuel exhaust gas cleans fusion agent and natural gas after the atomization of mixing chamber 2, is output to common rail pipe 5 through mixing tube 4, then with The burning output low pollution thermal energy of burner 9 is input to after air mixing.
The ratio of each propellant composition can be obtained by controlling each valve by controller, to obtain the heat of low pollution Energy.
Preferably, mixing chamber 2 is Venturi tube, the nozzle of 2 internal layer of mixing chamber is fine taper, the output of 2 outer layer of mixing chamber Mouth is big taper.
Preferably, mixing tube 4 is taper.
Fuel exhaust gas cleaning fusion agent is made from the following raw materials in parts by weight: 3.5 parts of the tert-butyl alcohol, 75 parts of methanol, toluene two 17 parts of isocyanates, 1.5 parts of oleic acid, 2.5 parts of dimethoxy-ethane, 1.5 parts of atoleine, 1.5 parts of naproanilide.
Method acquisition is prepared by the following procedure in fuel exhaust gas cleaning fusion agent:
3.5 parts of the tert-butyl alcohol is added 17 parts of toluene di-isocyanate(TDI)s and is sufficiently stirred by S1;
S2 adds after 1.5 parts of naproanilide stirrings sufficiently time of repose 15-25 minutes;
1.5 parts of oleic acid, 2.5 parts of dimethoxy-ethanes, 1.5 parts of atoleines are sequentially added stirring 10-20 minutes by S3;
The above deployed component is added in 75 parts of methanol components and is stirred 25-35 minutes by S4, still aging 1.5-2.5 hour is made fuel exhaust gas and cleans fusion agent.

Claims (5)

1. a kind of natural gas joint fuel exhaust gas cleans fusion agent high-pressure common rail premixing combustion apparatus, characterized in that include:
Natural gas motor regulated valve (1), input terminal are connected to high-pressure natural gas gas source;
Fuel exhaust gas cleans fusion agent motor regulated valve (3), and input terminal cleans fusion agent through hydraulic pump connection fuel exhaust gas Storage tank;
Mixing chamber (2) is double-layer structure, and the input port of internal layer is connected to the output end of natural gas motor regulated valve (1), outer layer Input port is connected to the delivery outlet of fuel exhaust gas cleaning fusion agent motor regulated valve (3);
Mixing tube (4), input port are connected to the delivery outlet of mixing chamber (2) internal layer and the delivery outlet of outer layer;
Common rail pipe (5), input port are connected to the delivery outlet of mixing tube (4);
Burner (9), is provided with multiple, is provided with gas-liquid mixed pipe (6) and combustion tube (8), gas-liquid mixed pipe (6) it is defeated Outlet is arranged in the combustion chamber of burner (9), and the delivery outlet of input terminal connection common rail pipe (5) of gas-liquid mixed pipe (6) helps The output end of combustion pipe (8) is arranged in the combustion chamber of burner (9), and the input terminal of combustion tube (8) is through air electric control valve Door connection air pump (7);
Controller, electrical connection natural gas motor regulated valve (1), fuel exhaust gas cleaning fusion agent motor regulated valve (3) and sky Gas motor regulated valve;
Fuel exhaust gas cleans fusion agent and natural gas after mixing chamber (2) are atomized, and is output to common rail pipe (5) through mixing tube (4), then Burner (9) burning output low pollution thermal energy is input to after mixing with air.
2. a kind of natural gas joint fuel exhaust gas as described in claim 1 cleans fusion agent high-pressure common rail premixing combustion apparatus, It is characterized in that the mixing chamber (2) is Venturi tube, the delivery outlet of mixing chamber (2) internal layer is fine taper, mixing chamber (2) outer layer Delivery outlet is big taper.
3. a kind of natural gas joint fuel exhaust gas as described in claim 1 cleans fusion agent high-pressure common rail premixing combustion apparatus, It is characterized in that the mixing tube (4) is taper.
4. a kind of natural gas joint fuel exhaust gas cleaning fusion agent high-pressure common rail premix combustion as described in any one of claims 1-3 Burn device, characterized in that the fuel exhaust gas cleaning fusion agent is made from the following raw materials in parts by weight: 3.5 parts of the tert-butyl alcohol, methanol 75 parts, 17 parts of toluene di-isocyanate(TDI), 1.5 parts of oleic acid, 2.5 parts of dimethoxy-ethane, 1.5 parts of atoleine, naproanilide 1.5 Part.
5. a kind of natural gas joint fuel exhaust gas as claimed in claim 4 cleans fusion agent high-pressure common rail premixing combustion apparatus, It is characterized in that method acquisition is prepared by the following procedure in the fuel exhaust gas cleaning fusion agent:
3.5 parts of the tert-butyl alcohol is added 17 parts of toluene di-isocyanate(TDI)s and is sufficiently stirred by S1;
S2 adds after 1.5 parts of naproanilide stirrings sufficiently time of repose 15-25 minutes;
1.5 parts of oleic acid, 2.5 parts of dimethoxy-ethanes, 1.5 parts of atoleines are sequentially added stirring 10-20 minutes by S3;
The above deployed component is added in 75 parts of methanol components and is stirred 25-35 minutes by S4, still aging 1.5- Obtained fuel exhaust gas cleans fusion agent within 2.5 hours.
CN201811181061.7A 2018-10-11 2018-10-11 Natural gas combines fuel exhaust gas and cleans fusion agent high-pressure common rail premixing combustion apparatus Active CN109373336B (en)

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Publication number Priority date Publication date Assignee Title
CN110186186A (en) * 2019-04-24 2019-08-30 大庆百世环保科技开发有限公司 It is a kind of can multifuel combustion on-condensible gas hot wind furnace technology

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000023542A1 (en) * 1998-10-16 2000-04-27 Mobil Oil Australia Pty Ltd Automotive liquefied petroleum gas (lpg) detergent additive composition
CN102182558A (en) * 2009-12-15 2011-09-14 通用电气公司 System and method of improving emission performance of a gas turbine
CN103468339A (en) * 2013-09-17 2013-12-25 郑海昌 Natural gas combustion synergist, natural gas mixture containing same, and preparation method of natural gas mixture
CN103710062A (en) * 2014-01-02 2014-04-09 北京大通鸿业科技发展有限公司 Efficient natural gas
CN106800954A (en) * 2016-12-22 2017-06-06 淄博津昌助燃材料科技有限公司 A kind of clean fuel oil additive and use its fuel oil
CN206549876U (en) * 2017-03-07 2017-10-13 石嘴山市讯通实业有限责任公司 Natural gas additive atomizer

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2000023542A1 (en) * 1998-10-16 2000-04-27 Mobil Oil Australia Pty Ltd Automotive liquefied petroleum gas (lpg) detergent additive composition
CN102182558A (en) * 2009-12-15 2011-09-14 通用电气公司 System and method of improving emission performance of a gas turbine
CN103468339A (en) * 2013-09-17 2013-12-25 郑海昌 Natural gas combustion synergist, natural gas mixture containing same, and preparation method of natural gas mixture
CN103710062A (en) * 2014-01-02 2014-04-09 北京大通鸿业科技发展有限公司 Efficient natural gas
CN106800954A (en) * 2016-12-22 2017-06-06 淄博津昌助燃材料科技有限公司 A kind of clean fuel oil additive and use its fuel oil
CN206549876U (en) * 2017-03-07 2017-10-13 石嘴山市讯通实业有限责任公司 Natural gas additive atomizer

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