CN104312634A - Composite thermal oxidative nozzle and application thereof - Google Patents

Composite thermal oxidative nozzle and application thereof Download PDF

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Publication number
CN104312634A
CN104312634A CN201410527711.4A CN201410527711A CN104312634A CN 104312634 A CN104312634 A CN 104312634A CN 201410527711 A CN201410527711 A CN 201410527711A CN 104312634 A CN104312634 A CN 104312634A
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China
Prior art keywords
jet pipe
shroud
nozzle
vaporized chemical
shroud jet
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CN201410527711.4A
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Chinese (zh)
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CN104312634B (en
Inventor
郭庆华
王涛
于广锁
龚欣
王辅臣
刘海峰
王亦飞
马奕
龚岩
颜卓勇
代正华
周志杰
陈雪莉
王兴军
梁钦锋
李伟锋
郭晓镭
许建良
陆海峰
赵辉
李超
范普兴
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华东理工大学
普莱克斯技术有限公司
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Publication of CN104312634A publication Critical patent/CN104312634A/en
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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/48Apparatus; Plants
    • C10J3/50Fuel charging devices
    • C10J3/506Fuel charging devices for entrained flow gasifiers
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J3/00Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
    • C10J3/46Gasification of granular or pulverulent flues in suspension
    • C10J3/54Gasification of granular or pulverulent fuels by the Winkler technique, i.e. by fluidisation
    • C10J3/56Apparatus; Plants
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2200/00Details of gasification apparatus
    • C10J2200/15Details of feeding means
    • C10J2200/152Nozzles or lances for introducing gas, liquids or suspensions
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10JPRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
    • C10J2300/00Details of gasification processes
    • C10J2300/09Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
    • C10J2300/0913Carbonaceous raw material

Abstract

The invention discloses a composite thermal oxidative nozzle and application thereof. The thermal oxidative nozzle consists of three groups of gasifying agent channels, three groups of fuel channels and a cooling system, wherein the channels are coaxially arranged and are connected by flanges. The composite thermal oxidative nozzle provided by the invention can be used for igniting carbon-containing fuels such as a water-coal-slurry, pulverized coal and biomass at low temperatures, so that the igniting process of a gasifying furnace is simplified. Two thermal oxidative channels are arranged in the annular space and center, so that not only is the fuel atomizing effect intensified, are the mass and heat transfer effects and the chemical reaction rate enhanced and is the adjustable range of the gasifying agent and fuels increased, but also the composite thermal oxidative nozzle is conveniently matched with the furnace body to form a proper fluid field according to arrangement of nozzles. The nozzle disclosed by the invention has the advantages of excellent atomizing performance, high carbon conversion efficiency, wide application range, long service life and the like and has very wide application prospect.

Description

A kind of combined type heat oxygen nozzle and application thereof

Technical field

The invention belongs to gasification field, relate to a kind of novel combined hot oxygen nozzle, particularly relate to for the carbonaceous material such as coal water slurry and fine coal vaporizing system for synthetic gas (CO+H 2).

Background technology

Gasification is the important channel of developing clean coal technology.Wherein, coal adaptability is strong because having for entrained flow bed gasification technology, throughput and gasification efficiency advantages of higher, worldwide obtains and promotes rapidly and apply widely.According to the difference of feed-type, airflow bed gasification furnace can be divided into two classes: a class is dry method feed, and coal dust is directly air conveying to nozzle, and representing the type of furnace is Shell; Another kind of is wet method feed, and water-coal slurry pump is delivered to nozzle, and representing the type of furnace is OMB and Texaco.Wherein, nozzle is all indispensable key part of two kinds of type of furnaces, and its life-span and function directly determine the safety and stability long-term operation of airflow bed gasification furnace.

First coal slurry gasifier ignition process adopts pre-hot nozzle furnace temperature to be risen to more than 1000 DEG C and constant temperature, then Replacement procedure nozzle feeds intake.Powder coal gasification furnace (for Shell) is first lighted a fire by ignition burner, then by the nozzle that goes into operation, vapourizing furnace is preheating to high-temperature high-pressure state, finally starts technique nozzle and feeds intake.In ignition process, the two all needs to consume a large amount of energy to promote fire box temperature, moreover because need in ignition process repeatedly to change nozzle, therefore its operation relative complex, the time of driving is longer, is unfavorable for the continuous and steady operation of device in Chemical Manufacture.

Gasification nozzle should ensure that good atomizing effect promotes mixing of fuel and vaporized chemical, mate again forms suitable flow field with body of heater, and then the temperature distribution that formation is suitable for, and reaches the object protecting nozzle, refractory brick.Disclosed in Chinese patent 102977926A and 102767827A, hot oxygen nozzle is applicable to the carbonaceous fuels such as solid powder fuel and coal water slurry respectively, both all adopt annular space to lead to hot oxygen, center leads to the structure of fuel, the direct ignition to fuel can be realized, although hot oxygen at a high speed to a certain extent can the atomizing effect of enhanced fuel, because only have the hot oxygen in annular space one tunnel, so the adjustable extent of vaporized chemical and fuel flow is narrower, be unfavorable for that the long period stability of vapourizing furnace is run.

Summary of the invention

In view of above problem, the invention provides a kind of combined type heat oxygen nozzle and the application in vapourizing furnace thereof, for the airflow bed gasification furnace being raw material with the carbonaceous material such as coal water slurry or fine coal, this nozzle can simplify driving and the operation of existing gasifying process, relative to existing nozzle, this hot oxygen nozzle adopts annular space and the hot oxygen of center two-way, pre-mixing is carried out compared with the central hot oxygen of lower velocity and middle ring fuel by high temperature, both mixing of fuel and vaporized chemical had been enhanced, tentatively improve fuel temperature, also can not produce larger wearing and tearing to jet pipe, the hot oxygen of outer shroud of high temperature and high speed shears atomization consumingly to ring fuel in pre-mixing, and can fire fuel rapidly, by regulating outer shroud, center fuel flow and vaporized chemical flow and hot oxygen chamber length, can regulate the length of the temperature of hot oxygen and speed and hot oxygen flame 22 (as shown in Figure 1), the change of outer shroud pipeline four and outer shroud pipeline five head construction can change the width of flame, therefore, the setting of annular space and the hot oxygen of center two-way had both enhanced the atomization of nozzle, in turn increase the adjustable extent of vaporized chemical and fuel, thus can according to the layout of nozzle, mate with body of heater comparatively easily and form suitable flow field.

Realize the technical scheme of the object of the invention:

A kind of combined type heat oxygen nozzle, described combined type heat oxygen nozzle comprises from outside to inside coaxial outer shroud jet pipe one, outer shroud jet pipe two, outer shroud jet pipe three, outer shroud jet pipe four, outer shroud jet pipe five, the core jet pipe arranged successively, and vaporized chemical passage, fuel channel, hot oxygen chamber and cooling system;

The inner ring vaporized chemical passage that during the outer shroud vaporized chemical passage that described vaporized chemical passage is made up of described outer shroud jet pipe one and described outer shroud jet pipe two, described outer shroud jet pipe three and described outer shroud jet pipe four are formed, ring vaporized chemical passage and described outer shroud jet pipe five and described core jet pipe are formed forms;

The center fuel passage that during the outer shroud fuel channel that described fuel channel is made up of described outer shroud jet pipe two and outer shroud jet pipe three, described outer shroud jet pipe four and outer shroud jet pipe five are formed, ring fuel channel and described core jet pipe are formed forms; The end that described outer shroud jet pipe four is recessed in described hot oxygen nozzle fully mixes with the gaseous media of center fuel passage with ring fuel channel exit in guarantee;

The head of described outer shroud jet pipe two, outer shroud jet pipe three and core jet pipe all adopts straight tube structure, and keeps same indent with spray nozzle front end vertically, to ensure the hot oxygen cavity space that hot oxygen is enough;

Described cooling system comprises spiral coil cooling tube and cooling room, and described spiral coil cooling tube is symmetricly set in the head of described combined type heat oxygen nozzle along described core jet pipe, and described cooling room is coaxially arranged at outside the head of described outer shroud pipeline one.

Cooling room is connected with spiral coil cooling tube, and cooling fluid flows out through coil pipe after flowing into cooling room again.

Described hot oxygen chamber comprises the hot oxygen chamber of outer shroud and central hot oxygen chamber; Described outer shroud hot oxygen chamber is formed at the head of described combined type heat oxygen nozzle by described outer shroud jet pipe one, outer shroud jet pipe two, outer shroud jet pipe three, outer shroud jet pipe four, and described central hot oxygen chamber is formed at the head of described combined type heat oxygen nozzle by described outer shroud jet pipe five and described core jet pipe.

The length of described outer shroud hot oxygen chamber and the indent t1 of outer shroud jet pipe two and outer shroud jet pipe three are 1 ~ 5 times of described outer shroud fuel channel equivalent diameter, and the described length of central hot oxygen chamber and the indent t2 of core jet pipe are 1 ~ 6 times of described center fuel passage equivalent diameter.

The head of described outer shroud jet pipe four adopts straight tube structure or tapered configuration; The head of described outer shroud jet pipe five adopts straight tube structure or tapered configuration, inwardly shrinks 0 ~ 20mm; Further, the head of described outer shroud jet pipe four keeps concordant with the head of described outer shroud jet pipe one.

When the head of described outer shroud jet pipe four adopts tapered configuration, flare oblique angle α is 45 ~ 80 °, and interior angle of throat θ is 45 ~ 80 °;

When the head of described outer shroud jet pipe five adopts tapered configuration, flare oblique angle γ is 45 ~ 80 °, and interior angle of throat δ is 45 ~ 80 °.

The interior angle of throat β of the head of described outer shroud jet pipe one is 30 ~ 80 °.

Flare oblique angle is the angle of jet pipe outer rim and nozzle face, and interior angle of throat is the angle of jet pipe inner edge and nozzle centre axis.

Described outer shroud jet pipe one, outer shroud jet pipe two, outer shroud jet pipe three, outer shroud jet pipe four, outer shroud jet pipe five, core jet pipe are all arranged by flange coaxial, ensure concentricity between each jet pipe by six pieces of double-deck uniform preset piecess.

The gasification dosage entering outer shroud vaporized chemical passage and middle ring vaporized chemical passage accounts for 80 ~ 95% of vaporized chemical total amount altogether, and the gasification dosage of its outer-loop and middle ring vaporized chemical passage is consistent, and inner ring vaporized chemical passage accounts for 5 ~ 20% of vaporized chemical total amount; In outer shroud fuel channel, fuel flow accounts for the ratio of outer shroud and middle ring vaporized chemical total amount is 2 ~ 20%, and in center fuel passage, fuel flow accounts for the ratio of inner ring vaporized chemical flow is 2 ~ 20%.

The vaporized chemical flow velocity of described outer shroud vaporized chemical passage and middle ring vaporized chemical passage is equal, be 0 ~ 50m/s, in described outer shroud fuel channel, fuel flow rate is 0 ~ 50m/s, the exit carbonaceous material flow velocity of described middle ring fuel channel is 0.1 ~ 1.0m/s, and the flow velocity of outer shroud hot oxygen chamber and the hot vaporized chemical of central hot oxygen chamber is respectively 20 ~ 600m/s and 20 ~ 250m/s;

Fuel in outer shroud fuel channel and center fuel passage is selected from one or more in Sweet natural gas, methane, propane, synthetic gas, coke(oven)gas, periodic off-gases, and the fuel in middle ring fuel channel is selected from one or more in coal water slurry, fine coal, Sweet natural gas, coke(oven)gas.

The application of above-mentioned arbitrary described combined type heat oxygen nozzle, described hot oxygen nozzle is arranged on airflow bed gasification furnace, body of heater top or certain plane of body of heater periphery or multiple plane arrange this nozzle one or more, for with coal water slurry or fine coal for synthetic gas prepared by raw material, produce the gasification process of synthetic ammonia, methyl alcohol, combined cycle generation, sponge iron or rubbish.

Containing the vapourizing furnace of above-mentioned arbitrary described hot oxygen nozzle, the top of described vapourizing furnace or a plane of body of heater periphery or multiple plane are provided with one or more described hot oxygen nozzle.

Hot oxygen nozzle of the present invention can put the carbonaceous fuels such as combusting coal water slurry, fine coal, biomass at low temperatures, thus simplifies vapourizing furnace ignition process.The setting of annular space and the hot oxygen of center two-way not only enhances fuel atomizing effect, mass-and heat-transfer effect and chemical reaction rate are improved, and increase the adjustable extent of vaporized chemical and fuel, thus according to the layout of nozzle, conveniently can mate with body of heater and form suitable flow field.The advantages such as the present invention has that atomization is excellent, efficiency of carbon conversion is high, applied widely, long service life, have very wide application prospect.

Accompanying drawing explanation

Fig. 1 is the agent structure sectional view of the combined type heat oxygen nozzle of embodiment 1;

Fig. 2 is the head construction sectional view of the combined type heat oxygen nozzle of embodiment 1.

Nomenclature

1 spiral coil cooling tube; 2 preset piecess; 3 outer shroud jet pipes one; 4 outer shroud jet pipes two;

5 outer shroud jet pipes three; 6 outer shroud jet pipes four; 7 outer shroud jet pipes five; 8 core jet pipes;

9 flanges; Ring vaporized chemical passage in 10; Ring fuel channel in 11; 12 inner ring gasification agent inlets;

13 outer shroud fuel inlets; 14 outer shroud gasification agent inlets; The outlet of ring fuel channel 20 in 15;

16 outer shroud vaporized chemical passages; Ring vaporized chemical passage in 17; 18 inner ring vaporized chemical passages;

19 center fuel passages; Ring fuel channel in 20; 21 outer shroud fuel channels;

22 hot oxygen flames; The hot oxygen chamber of 23 outer shroud; 24 central hot oxygen chambers;

The head of 25 outer shroud jet pipes four; The head of 26 outer shroud jet pipes five; The hot oxygen outlet of 27 annular space;

The head of 28 outer shroud jet pipes one; 29 cooling rooms.

Embodiment

Below, further illustrate content of the present invention by embodiment, but protection scope of the present invention is not limited in embodiment.To the other changes and modifications that those skilled in the art makes when not deviating from the present invention's spirit and protection domain, be still included within scope.

Fig. 1 is the structural representation of combined type heat oxygen nozzle of the present invention, and Fig. 2 is combined type heat oxygen nozzle head structural representation.Hot oxygen nozzle of the present invention comprises outer shroud jet pipe 1, outer shroud jet pipe 24, outer shroud jet pipe 35, outer shroud jet pipe 46, outer shroud jet pipe 57, core jet pipe 8 and cooling system, each jet pipe adopts Flange joint and coaxial setting successively, ensures concentricity between jet pipe by double-deck six pieces of uniform preset piecess 2.

Cooling system is made up of spiral coil cooling tube 1 and cooling room 29.Cooling room is coaxially arranged at the outside of outer shroud pipeline one head 28.Cooling fluid flows out through spiral coil cooling tube 1 after entering cooling room 29 again.

The head of outer shroud jet pipe 24, outer shroud jet pipe 35 and core jet pipe 8 all adopts straight tube structure, and keep certain indent with spray nozzle front end vertically, thus form the hot oxygen chamber 23 of outer shroud and central hot oxygen chamber 24 with outer shroud jet pipe 1 and outer shroud jet pipe 46 and outer shroud jet pipe 57 respectively.

The length t1 of the hot oxygen chamber 23 of outer shroud is 1 ~ 5 times of outer shroud fuel channel 21 equivalent diameter, 1 ~ 6 times of fuel channel 19 equivalent diameter centered by the length t2 of central hot oxygen chamber.

The head 25 of outer shroud jet pipe 46 adopts straight tube structure or tapered configuration, and it keeps concordant with the head 28 of outer shroud jet pipe 1, and flare oblique angle α when adopting tapered configuration is 45 ~ 80 °, and interior contraction half-angle θ is 45 ~ 80 °; The head 26 of outer shroud jet pipe 57 adopts straight tube structure or tapered configuration, inwardly shrinks 0 ~ 20mm, and flare oblique angle γ when adopting tapered configuration is 45 ~ 80 °, and interior contraction half-angle δ is 45 ~ 80 °; The interior angle of throat β of the head 28 of outer shroud jet pipe 1 is 30 ~ 80 °.

Embodiment 1

Hot oxygen nozzle described in installing at vertical top of gasification furnace take solid content as the coal water slurry of 61% is fuel, and the oxygen with 99.8% is vaporized chemical, and the methane with 99% is combustion gas, and coal water slurry flow is 10kg/h, combustion gas: vaporized chemical=10%, and oxygen flow is 4.8Nm 3/ h, vapor pressure is normal pressure, and refractory liner adopts refractory brick, and gasification temperature is about 1300 DEG C, and vaporizer height is 2.2m, and vaporizer internal diameter is 0.3m.

Coal water slurry therefrom ring fuel inlet enters middle ring fuel channel, oxygen divides three tunnels to enter outer shroud vaporized chemical passage, middle ring vaporized chemical passage and inner ring vaporized chemical passage by outer shroud, middle ring and inner ring gasification agent inlet respectively, the ratio of each passage oxygen flow is 45:45:10, methane divides two-way to enter outer shroud and center fuel passage by outer shroud and center fuel entrance respectively, and each passage ratio is 9:1.Total oxygen demand is excessive in stoichiometry relative to oxygen required during methane perfect combustion, and excessive oxygen is heated to about 1500 DEG C and flows out from hot oxygen chamber outlet in hot oxygen chamber.The oxygen gas flow rate of outer shroud, middle ring and inner ring vaporized chemical passage is 30m/s, in outer shroud and center fuel passage, methane gas speed is 20m/s, in middle ring fuel channel, coal water slurry exit velocity is 0.3m/s, and the hot oxygen gas flow rate of annular space and central hot oxygen chamber outlet is respectively about 200m/s and about 400m/s.

Ignition phase, first lights central hot oxygen, and then utilizes central hot oxygen point to fire the hot oxygen of annular space.Carbonaceous material in inner ring fuel channel to enter after nozzle first with central hot oxygen generation pre-mixing, temperature of charge raises, the hot oxygen of annular space being subject to high temperature and high speed after delivery nozzle shears atomization consumingly, is lighted rapidly, and at the burning of nozzle generating portion and gasification reaction.When furnace temperature rises to about 1000 DEG C or more, can cut off methane supply, hot oxygen nozzle can use by gasifying process nozzle conveniently.Experimental result shows, the hot oxygen that this nozzle is formed directly can put combusting coal water slurry, and the flame forms of formation is even, stable, the efficiency of carbon conversion of feed coal comparatively normal temperature oxygen jet mean height about 2 percentage points under the same reaction time.

If when there is the damage such as cinder notch slagging scorification, wall dross in actual production process in vapourizing furnace, again can cutting into outer shroud or center fuel passage methane, light hot oxygen flame, eliminating slagging scorification by regulating hot oxygen flame.When there is fluctuation in coal slurry feed or needs to improve production load, also can by the optimization regulating hot oxygen flame temperature to realize oxygen coal ratio.

Combined type heat oxygen nozzle of the present invention is adopted in above-mentioned example, the carbonaceous materials such as coal water slurry can complete vapourizing furnace igniting under lower fire box temperature, simplify the ignition process of airflow bed gasification furnace greatly, save a large amount of fuel and vaporized chemical that heat up for vapourizing furnace.High-temperature oxygen jet flame can not only significantly improve heat and mass speed, and then improves the efficiency of carbon conversion of fuel, and also can play the function of improvement for the damage occurred in actual production.

Although the foregoing describe the specific embodiment of the present invention, it will be understood by those of skill in the art that these only illustrate, protection scope of the present invention is defined by the appended claims.Those skilled in the art, under the prerequisite not deviating from principle of the present invention and essence, can make various changes or modifications to these embodiments, but these change and amendment all falls into protection scope of the present invention.

Claims (10)

1. a combined type heat oxygen nozzle, it is characterized in that, described combined type heat oxygen nozzle comprises from outside to inside coaxial outer shroud jet pipe one, outer shroud jet pipe two, outer shroud jet pipe three, outer shroud jet pipe four, outer shroud jet pipe five, the core jet pipe arranged successively, and vaporized chemical passage, fuel channel, hot oxygen chamber and cooling system;
The inner ring vaporized chemical passage that during the outer shroud vaporized chemical passage that described vaporized chemical passage is made up of described outer shroud jet pipe one and described outer shroud jet pipe two, described outer shroud jet pipe three and described outer shroud jet pipe four are formed, ring vaporized chemical passage and described outer shroud jet pipe five and described core jet pipe are formed forms;
The center fuel passage that during the outer shroud fuel channel that described fuel channel is made up of described outer shroud jet pipe two and outer shroud jet pipe three, described outer shroud jet pipe four and outer shroud jet pipe five are formed, ring fuel channel and described core jet pipe are formed forms; Described outer shroud jet pipe four is recessed in the end of described hot oxygen nozzle;
The head of described outer shroud jet pipe two, outer shroud jet pipe three and core jet pipe all adopts straight tube structure, and keeps same indent with spray nozzle front end vertically;
Described cooling system comprises spiral coil cooling tube and cooling room, and described spiral coil cooling tube is symmetricly set in the head of described combined type heat oxygen nozzle along described core jet pipe, and described cooling room is coaxially arranged at outside the head of described outer shroud pipeline one.
2. combined type heat oxygen nozzle according to claim 1, is characterized in that, described hot oxygen chamber comprises the hot oxygen chamber of outer shroud and central hot oxygen chamber; Described outer shroud hot oxygen chamber is formed at the head of described combined type heat oxygen nozzle by described outer shroud jet pipe one, outer shroud jet pipe two, outer shroud jet pipe three, outer shroud jet pipe four, and described central hot oxygen chamber is formed at the head of described combined type heat oxygen nozzle by described outer shroud jet pipe five and described core jet pipe.
3. combined type heat oxygen nozzle according to claim 2, it is characterized in that, the length t1 of described outer shroud hot oxygen chamber is 1 ~ 5 times of described outer shroud fuel channel equivalent diameter, and the length t2 of described central hot oxygen chamber is 1 ~ 6 times of described center fuel passage equivalent diameter.
4. combined type heat oxygen nozzle according to claim 3, is characterized in that, the head of described outer shroud jet pipe four adopts straight tube structure or tapered configuration; The head of described outer shroud jet pipe five adopts straight tube structure or tapered configuration, inwardly shrinks 0 ~ 20mm; Further, the head of described outer shroud jet pipe four keeps concordant with the head of described outer shroud jet pipe one.
5. combined type heat oxygen nozzle according to claim 4, is characterized in that, when the head of described outer shroud jet pipe four adopts tapered configuration, flare oblique angle α is 45 ~ 80 °, and interior angle of throat θ is 45 ~ 80 °;
When the head of described outer shroud jet pipe five adopts tapered configuration, flare oblique angle γ is 45 ~ 80 °, and interior angle of throat δ is 45 ~ 80 °.
6. combined type heat oxygen nozzle according to claim 4, is characterized in that, the interior angle of throat β of the head of described outer shroud jet pipe one is 30 ~ 80 °.
7. according to the arbitrary described combined type heat oxygen nozzle of claim 1 ~ 6, it is characterized in that, described outer shroud jet pipe one, outer shroud jet pipe two, outer shroud jet pipe three, outer shroud jet pipe four, outer shroud jet pipe five, core jet pipe are all arranged by flange coaxial, ensure concentricity between each jet pipe by six pieces of double-deck uniform preset piecess.
8. combined type heat oxygen nozzle according to claim 7, it is characterized in that, the gasification dosage entering outer shroud vaporized chemical passage and middle ring vaporized chemical passage accounts for 80 ~ 95% of vaporized chemical total amount altogether, the gasification dosage of its outer-loop and middle ring vaporized chemical passage is consistent, and inner ring vaporized chemical passage accounts for 5 ~ 20% of vaporized chemical total amount; In outer shroud fuel channel, fuel flow accounts for the ratio of outer shroud and middle ring vaporized chemical total amount is 2 ~ 20%, and in center fuel passage, fuel flow accounts for the ratio of inner ring vaporized chemical flow is 2 ~ 20%.
9. combined type heat oxygen nozzle according to claim 7, it is characterized in that, the vaporized chemical flow velocity of described outer shroud vaporized chemical passage and middle ring vaporized chemical passage is equal, be 0 ~ 50m/s, in described outer shroud fuel channel, fuel flow rate is 0 ~ 50m/s, the exit carbonaceous material flow velocity of described middle ring fuel channel is 0.1 ~ 1.0m/s, and the flow velocity of outer shroud hot oxygen chamber and the hot vaporized chemical of central hot oxygen chamber is respectively 20 ~ 600m/s and 20 ~ 250m/s;
Fuel in outer shroud fuel channel and center fuel passage is selected from one or more in Sweet natural gas, methane, propane, synthetic gas, coke(oven)gas, periodic off-gases, and the fuel in middle ring fuel channel is selected from one or more in coal water slurry, fine coal, Sweet natural gas, coke(oven)gas.
10. the application of the arbitrary described combined type heat oxygen nozzle of claim 1 ~ 9, it is characterized in that, described hot oxygen nozzle is arranged on airflow bed gasification furnace, body of heater top or certain plane of body of heater periphery or multiple plane arrange this nozzle one or more, for with coal water slurry or fine coal for synthetic gas prepared by raw material, produce the gasification process of synthetic ammonia, methyl alcohol, combined cycle generation, sponge iron or rubbish.
CN201410527711.4A 2014-10-09 2014-10-09 A kind of combined type Hot oxygen nozzle and its application CN104312634B (en)

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Cited By (4)

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Publication number Priority date Publication date Assignee Title
CN105112104A (en) * 2015-09-14 2015-12-02 西北化工研究院 Multichannel nozzle used for multi-component slurry gasification reactor and application of multichannel nozzle
CN105694981A (en) * 2016-02-19 2016-06-22 新奥科技发展有限公司 Gasifier nozzle and gasifier
WO2017032319A1 (en) * 2015-08-26 2017-03-02 上海泽玛克敏达机械设备有限公司 Multi-functional nozzle for fixed bed slag gasification furnace, and fixed bed slag gasification furnace
CN108913215A (en) * 2018-08-06 2018-11-30 唐山科源环保技术装备有限公司 Remove ammonia and the technique for carrying out innocuously transformation processing in producer gas

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CN105694981A (en) * 2016-02-19 2016-06-22 新奥科技发展有限公司 Gasifier nozzle and gasifier
CN105694981B (en) * 2016-02-19 2019-02-05 新奥科技发展有限公司 A kind of gasifying furnace nozzle and gasification furnace
CN108913215A (en) * 2018-08-06 2018-11-30 唐山科源环保技术装备有限公司 Remove ammonia and the technique for carrying out innocuously transformation processing in producer gas

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