CN115234899A - A heat carrier heating furnace for burning biomass to make gas - Google Patents

A heat carrier heating furnace for burning biomass to make gas Download PDF

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CN115234899A
CN115234899A CN202210889488.2A CN202210889488A CN115234899A CN 115234899 A CN115234899 A CN 115234899A CN 202210889488 A CN202210889488 A CN 202210889488A CN 115234899 A CN115234899 A CN 115234899A
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combustion chamber
convection section
furnace body
biomass
heat carrier
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张金庆
丁宏
唐翌群
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CHANGZHOU ENERGY ENGINEERING CO LTD
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CHANGZHOU ENERGY ENGINEERING CO LTD
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    • 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 
    • F23C9/00Combustion apparatus characterised by arrangements for returning combustion products or flue gases to the combustion chamber
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23JREMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES 
    • F23J15/00Arrangements of devices for treating smoke or fumes
    • F23J15/06Arrangements of devices for treating smoke or fumes of coolers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23MCASINGS, LININGS, WALLS OR DOORS SPECIALLY ADAPTED FOR COMBUSTION CHAMBERS, e.g. FIREBRIDGES; DEVICES FOR DEFLECTING AIR, FLAMES OR COMBUSTION PRODUCTS IN COMBUSTION CHAMBERS; SAFETY ARRANGEMENTS SPECIALLY ADAPTED FOR COMBUSTION APPARATUS; DETAILS OF COMBUSTION CHAMBERS, NOT OTHERWISE PROVIDED FOR
    • F23M11/00Safety arrangements

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  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Incineration Of Waste (AREA)

Abstract

本发明公开了一种燃生物质制气的热载体加热炉,具体涉及工业锅炉领域,包括炉体和燃烧室,所述燃烧室设置于炉体下方,所述燃烧室的一侧设置有燃烧器,所述炉体内部远离燃烧器的一侧底端安装有辐射段盘管,所述辐射段盘管的上端连接有顶棚管,所述炉体的内部位于辐射段盘管和顶棚管的一侧设置有对流段,所述炉体的外端设置有进口集管,所述进口集管的一端设置于炉体内部连接有对流段集管,所述炉体的上端设置有出口集管和出烟口。本发明适应各类生物质制气燃料,保证稳定燃烧。采用绝热燃烧室,对各类热值低、含水量高、焦油含量高的气体,燃烧室温度始终保持在1000~1100℃之间,燃尽率高、氮氧化物产生量小。

Figure 202210889488

The invention discloses a heat carrier heating furnace for burning biomass to produce gas, in particular to the field of industrial boilers, comprising a furnace body and a combustion chamber, the combustion chamber is arranged below the furnace body, and a combustion chamber is arranged on one side of the combustion chamber A radiant section coil is installed at the bottom end of the side of the furnace body away from the burner, the upper end of the radiant section coil is connected with a ceiling tube, and the interior of the furnace body is located between the radiant section coil and the ceiling tube. A convection section is arranged on one side, an inlet header is arranged at the outer end of the furnace body, one end of the inlet header is arranged inside the furnace body and is connected with a convection section header, and the upper end of the furnace body is arranged with an outlet header and smoke outlet. The invention adapts to various biomass gas-making fuels and ensures stable combustion. The adiabatic combustion chamber is adopted, and the temperature of the combustion chamber is always kept between 1000 and 1100 °C for all kinds of gases with low calorific value, high water content and high tar content, with high burnout rate and low nitrogen oxide production.

Figure 202210889488

Description

一种燃生物质制气的热载体加热炉A heat carrier heating furnace for burning biomass to make gas

技术领域technical field

本发明涉及工业锅炉技术领域,更具体地说,本发明涉及一种燃生物质制气的热载体加热炉。The present invention relates to the technical field of industrial boilers, and more particularly, to a heat carrier heating furnace for burning biomass to produce gas.

背景技术Background technique

目前,随着国家碳达峰、碳中和的目标不断推进,生物质燃料得到大力发展;但生物质燃料来源的多样性和不稳定性,导致直燃生物质燃料加热炉的出力和污染物排放无法保证稳定,生物质制气作为燃料的加热炉得到应用。At present, with the continuous advancement of the national goal of carbon peaking and carbon neutrality, biomass fuels have been vigorously developed; however, the diversity and instability of biomass fuel sources have led to the output and pollutants of direct-fired biomass fuel heating furnaces. Emissions cannot be guaranteed to be stable, and biomass-to-gas heating furnaces are used as fuel.

生物质制气成分相对稳定、供应连续、调节方便,但同天然气、液化石油气、焦炉煤气等相比,又存在热值低、含水量高、焦油含量高的特点。同时,各制气厂家产生的气源品质也相差较大,燃生物质制气的热载体加热炉需要进行针对性设计。Compared with natural gas, liquefied petroleum gas and coke oven gas, biomass gas has relatively stable components, continuous supply and convenient adjustment. However, it has the characteristics of low calorific value, high water content and high tar content. At the same time, the quality of the gas source produced by various gas manufacturers is also quite different, and the heat carrier heating furnace burning biomass gas needs to be designed in a targeted manner.

申请内容Application content

为了克服现有技术的上述缺陷,本发明的实施例提供一种燃生物质制气的热载体加热炉,本发明所要解决的技术问题是:如何更好的利用生物质制气,提高生物质制气的利用效率。In order to overcome the above-mentioned defects of the prior art, an embodiment of the present invention provides a heat carrier heating furnace for burning biomass for gas production. The technical problem to be solved by the present invention is: how to better utilize biomass for gas production, improve biomass production Gas utilization efficiency.

为实现上述目的,本发明提供如下技术方案:一种燃生物质制气的热载体加热炉,包括炉体和燃烧室,所述燃烧室设置于炉体下方,所述燃烧室的一侧设置有燃烧器,所述炉体内部远离燃烧器的一侧底端安装有辐射段盘管,所述辐射段盘管的上端连接有顶棚管,所述炉体的内部位于辐射段盘管和顶棚管的一侧设置有对流段,所述炉体的外端设置有进口集管,所述进口集管的一端设置于炉体内部连接有对流段集管,所述炉体的上端设置有出口集管和出烟口。In order to achieve the above purpose, the present invention provides the following technical solutions: a heat carrier heating furnace for burning biomass to produce gas, comprising a furnace body and a combustion chamber, the combustion chamber is arranged below the furnace body, and one side of the combustion chamber is arranged There is a burner, and the bottom end of the side of the furnace body away from the burner is installed with a radiant section coil, the upper end of the radiant section coil is connected with a ceiling tube, and the interior of the furnace body is located between the radiant section coil and the ceiling. One side of the tube is provided with a convection section, the outer end of the furnace body is provided with an inlet header, one end of the inlet header is provided inside the furnace body and is connected with a convection section header, and the upper end of the furnace body is provided with an outlet Header and smoke outlet.

在一个优选的实施方式中,所述燃烧室的侧壁上开设有燃烧器接口,所述燃烧器安装在燃烧器接口处,所述燃烧器为高温型低氮燃气燃烧器,且所述燃烧器上设置有多级燃气紧急切断装置和泄放装置,燃烧器能够点燃燃烧室内部的生物质制气,设置多级燃气紧急切断装置和泄放装置能够有效提高生物炉的安全性。In a preferred embodiment, a burner interface is provided on the side wall of the combustion chamber, the burner is installed at the burner interface, the burner is a high-temperature low-nitrogen gas burner, and the combustion A multi-stage gas emergency cut-off device and a relief device are arranged on the burner, and the burner can ignite the biomass gas inside the combustion chamber. The multi-stage gas emergency shut-off device and the relief device can effectively improve the safety of the bio-furnace.

在一个优选的实施方式中,所述燃烧室采用负压燃烧,生物质气化装置制气后直接送燃烧室中燃烧,无需中间储罐和加压,生物质制气直接用于生物炉的燃烧,中间不需要其它工艺,工艺简单,成本较低。In a preferred embodiment, the combustion chamber adopts negative pressure combustion. After the biomass gasification device produces gas, it is directly sent to the combustion chamber for combustion without intermediate storage tanks and pressurization. Combustion, no other process is required in the middle, the process is simple, and the cost is low.

在一个优选的实施方式中,所述燃烧室的四周和下部均为绝热炉墙,燃烧室上部设置有炉拱和喉口,采用绝热燃烧室,对各类热值低、含水量高、焦油含量高的气体,燃烧室温度始终保持在1000-1100℃之间,燃尽率高、氮氧化物产生量小。In a preferred embodiment, the surrounding and lower parts of the combustion chamber are adiabatic furnace walls, and the upper part of the combustion chamber is provided with a furnace arch and a throat. With high content of gas, the temperature of the combustion chamber is always maintained between 1000-1100 ° C, the burnout rate is high, and the amount of nitrogen oxides produced is small.

在一个优选的实施方式中,所述对流段包括有第一对流段、第二对流段、第三对流段和第四对流段,所述第一对流段的一端辐射段盘管的一端连接,所述第四对流段的一端与对流段集管连接,多个对流段能够更好的实现热载体与生物炉内部热量的交换。In a preferred embodiment, the convection section includes a first convection section, a second convection section, a third convection section and a fourth convection section, and one end of the first convection section is connected to one end of the radiating section coil, One end of the fourth convection section is connected to the convection section header, and multiple convection sections can better realize the heat exchange between the heat carrier and the internal heat of the biological furnace.

在一个优选的实施方式中,所述第一对流段、第二对流段、第三对流段和第四对流段采用多级并联或串联结构,各级对流段随着烟气流动方向管片间距逐渐减小,根据炉体内部的实际实际可以选择性的将对流段设置为串联或并联结构。In a preferred embodiment, the first convective section, the second convective section, the third convective section and the fourth convective section adopt a multi-stage parallel or series structure, and the convection sections of each stage are spaced along the flue gas flow direction. It gradually decreases, and the convection section can be selectively set in series or parallel structure according to the actual situation inside the furnace body.

在一个优选的实施方式中,所述顶棚管远离辐射段盘管的一端与出口集管连接,热载体能够通过顶棚管进入到出口集管中,然后通过出口集管排出用于热设备放热。In a preferred embodiment, one end of the ceiling tube away from the radiant section coil is connected to the outlet header, and the heat carrier can enter the outlet header through the ceiling tube, and then be discharged through the outlet header for heat release of the thermal equipment .

与现有技术相比,本发明的技术效果和优点:Compared with the prior art, the technical effects and advantages of the present invention:

1、本发明适应各类生物质制气燃料,保证稳定燃烧。采用绝热燃烧室,对各类热值低、含水量高、焦油含量高的气体,燃烧室温度始终保持在 1000~1100℃之间,燃尽率高、氮氧化物产生量小;1. The present invention is suitable for all kinds of biomass gas-making fuels to ensure stable combustion. Adopting adiabatic combustion chamber, for all kinds of gases with low calorific value, high water content and high tar content, the temperature of the combustion chamber is always kept between 1000 and 1100 °C, the burnout rate is high, and the amount of nitrogen oxides produced is small;

2、本发明安全可靠,燃烧器带有多级燃气紧急切断和泄放装置,燃烧室为六面重型炉墙、设有防爆门,加热炉燃气燃烧安全可靠,事故损失小;2. The invention is safe and reliable, the burner is equipped with a multi-stage gas emergency cut-off and discharge device, the combustion chamber is a six-sided heavy furnace wall with explosion-proof doors, the heating furnace gas combustion is safe and reliable, and the accident loss is small;

3、本发明热效率高,生物质制气热值低,辐射换热少、对流换热多,采用辐射段+多级对流段结构,保证出烟温度≤热载体进口温度+20℃。3. The invention has high thermal efficiency, low calorific value of biomass gas production, less radiation heat exchange and more convection heat exchange, and adopts the structure of radiation section + multi-stage convection section to ensure that the temperature of the exhaust gas is less than or equal to the inlet temperature of the heat carrier + 20°C.

附图说明Description of drawings

图1为本发明的整体结构示意图。FIG. 1 is a schematic diagram of the overall structure of the present invention.

附图标记为:1、炉体;2、燃烧室;3、燃烧器;4、辐射段盘管;5、顶棚管;6、进口集管;7、对流段集管;8、出口集管;9、第一对流段;10、第二对流段;11、第三对流段;12、第四对流段。Reference signs are: 1. Furnace body; 2. Combustion chamber; 3. Burner; 4. Radiant section coil; 5. Ceiling tube; 6. Inlet header; 7. Convection section header; 8. Outlet header ; 9, the first convection section; 10, the second convection section; 11, the third convection section; 12, the fourth convection section.

具体实施方式Detailed ways

下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.

根据图1所示的一种燃生物质制气的热载体加热炉,包括炉体1和燃烧室2,所述燃烧室2设置于炉体1下方,所述燃烧室2的一侧设置有燃烧器3,所述炉体1内部远离燃烧器3的一侧底端安装有辐射段盘管4,所述辐射段盘管4的上端连接有顶棚管5,所述炉体1的内部位于辐射段盘管4和顶棚管5 的一侧设置有对流段,所述炉体1的外端设置有进口集管6,所述进口集管6 的一端设置于炉体1内部连接有对流段集管7,所述炉体1的上端设置有出口集管8和出烟口13。A heat carrier heating furnace for burning biomass to produce gas shown in FIG. 1 includes a furnace body 1 and a combustion chamber 2, the combustion chamber 2 is arranged below the furnace body 1, and one side of the combustion chamber 2 is provided with Burner 3, the bottom end of the furnace body 1 away from the burner 3 is installed with a radiant section coil 4, the upper end of the radiant section coil 4 is connected with a ceiling tube 5, and the interior of the furnace body 1 is located at A convection section is arranged on one side of the radiant section coil 4 and the ceiling tube 5, an inlet header 6 is arranged at the outer end of the furnace body 1, and one end of the inlet header 6 is arranged inside the furnace body 1 and is connected with a convection section. The header 7, the upper end of the furnace body 1 is provided with an outlet header 8 and a smoke outlet 13.

在一个优选的实施方式中,所述燃烧室2的侧壁上开设有燃烧器接口,所述燃烧器3安装在燃烧器接口处,所述燃烧器3为高温型低氮燃气燃烧器,且所述燃烧器3上设置有多级燃气紧急切断装置和泄放装置,燃烧器3能够点燃燃烧室2内部的生物质制气,设置多级燃气紧急切断装置和泄放装置能够有效提高生物炉的安全性。In a preferred embodiment, a burner interface is provided on the side wall of the combustion chamber 2, the burner 3 is installed at the burner interface, and the burner 3 is a high-temperature low-nitrogen gas burner, and The burner 3 is provided with a multi-stage gas emergency cut-off device and a discharge device, the burner 3 can ignite the biomass gas production in the combustion chamber 2, and the multi-stage gas emergency cut-off device and the discharge device can effectively improve the biological furnace. security.

在一个优选的实施方式中,所述燃烧室2采用负压燃烧,生物质气化装置制气后直接送燃烧室2中燃烧,无需中间储罐和加压,生物质制气直接用于生物炉的燃烧,中间不需要其它工艺,工艺简单,成本较低。In a preferred embodiment, the combustion chamber 2 adopts negative pressure combustion, and after the biomass gasification device produces gas, it is directly sent to the combustion chamber 2 for combustion without intermediate storage tanks and pressurization, and the biomass gas production is directly used for biological The combustion of the furnace does not require other processes in the middle, the process is simple, and the cost is low.

在一个优选的实施方式中,所述燃烧室3的四周和下部均为绝热炉墙,燃烧室3上部设置有炉拱和喉口,实际使用时燃烧室2处还设有防爆门、观火孔、人孔、检查孔等,提高设备的安全性能。In a preferred embodiment, the surrounding and lower parts of the combustion chamber 3 are thermally insulated furnace walls, the upper part of the combustion chamber 3 is provided with a furnace arch and a throat, and in actual use, the combustion chamber 2 is also provided with an explosion-proof door, a fire watch Holes, manholes, inspection holes, etc., to improve the safety performance of the equipment.

在一个优选的实施方式中,所述对流段包括有第一对流段9、第二对流段 10、第三对流段11和第四对流段12,所述第一对流段9的一端辐射段盘管4 的一端连接,所述第四对流段12的一端与对流段集管7连接,多个对流段能够更好的实现热载体与生物炉内部热量的交换。In a preferred embodiment, the convection section includes a first convection section 9, a second convection section 10, a third convection section 11 and a fourth convection section 12, and one end of the first convection section 9 radiates a section disc One end of the tube 4 is connected, and one end of the fourth convection section 12 is connected to the convection section header 7, and multiple convection sections can better realize the heat exchange between the heat carrier and the internal heat of the biological furnace.

在一个优选的实施方式中,所述第一对流段9、第二对流段10、第三对流段11和第四对流段12采用多级并联或串联结构,各级对流段随着烟气流动方向管片间距逐渐减小。In a preferred embodiment, the first convection section 9, the second convection section 10, the third convection section 11 and the fourth convection section 12 adopt a multi-stage parallel or series structure, and the convection sections of each level flow with the flue gas The directional segment spacing gradually decreases.

在一个优选的实施方式中,所述顶棚管5远离辐射段盘管4的一端与出口集管8连接,热载体能够通过顶棚管5进入到出口集管8中,然后通过出口集管8排出用于热设备放热。In a preferred embodiment, the end of the ceiling pipe 5 away from the radiant section coil 4 is connected to the outlet header 8 , and the heat carrier can enter the outlet header 8 through the ceiling pipe 5 and then be discharged through the outlet header 8 Used for heat release in thermal equipment.

实施方式具体为:使用时将生物质炉产生的生物质制气通过负压导入到燃烧室2中,利用燃烧器3将生物质制气点燃,生物质制气燃烧产生的热烟前部折向进入辐射段盘管2和顶棚管3外部,然后依次进入第一对流段9、第二对流段10、第三对流段11和第四对流段12,最后经过出烟口13排出,而热载体通过进口集管6导入,然后进入到对流段集管7中,使得热载体依次通过第四对流段12、第三对流段11、第二对流段10和第一对流段9,热载体在多个对流段中与炉体1中燃烧产生的热量进行热交换,第一对流段9中的热载体进入到辐射段盘管2中继续进行热交换,辐射段盘管2中的热载体进入到顶棚管3中,而顶棚管3中的热载体进入到出口集管8中,然后排出用于热设备发热。The specific embodiment is as follows: when in use, the biomass-made gas produced by the biomass furnace is introduced into the combustion chamber 2 through negative pressure, the biomass-made gas is ignited by the burner 3, and the hot smoke generated by the combustion of the biomass-made gas is folded at the front. To the outside of the radiant section coil 2 and the ceiling tube 3, and then enter the first convection section 9, the second convection section 10, the third convection section 11 and the fourth convection section 12 in turn, and finally exhaust through the smoke outlet 13, while the heat The carrier is introduced through the inlet header 6, and then enters the convection section header 7, so that the heat carrier passes through the fourth convection section 12, the third convection section 11, the second convection section 10 and the first convection section 9 in turn. Heat exchange is carried out with the heat generated by combustion in the furnace body 1 in the multiple convection sections. The heat carrier in the first convection section 9 enters the radiant section coil 2 to continue heat exchange, and the heat carrier in the radiant section coil 2 enters into the ceiling pipe 3, and the heat carrier in the ceiling pipe 3 enters into the outlet header 8, and then is discharged for heating of the thermal equipment.

本发明适应各类生物质制气燃料,保证稳定燃烧。采用绝热燃烧室,对各类热值低、含水量高、焦油含量高的气体,燃烧室温度始终保持在1000~1100℃之间,燃尽率高、氮氧化物产生量小;本发明安全可靠,燃烧器带有多级燃气紧急切断和泄放装置,燃烧室为六面重型炉墙、设有防爆门,加热炉燃气燃烧安全可靠,事故损失小;本发明热效率高,生物质制气热值低,辐射换热少、对流换热多,采用辐射段+多级对流段结构,保证出烟温度≤热载体进口温度+20℃。The invention adapts to various biomass gas-making fuels and ensures stable combustion. Adopting adiabatic combustion chamber, for all kinds of gases with low calorific value, high water content and high tar content, the temperature of the combustion chamber is always kept between 1000 and 1100°C, the burnout rate is high, and the amount of nitrogen oxides produced is small; the invention is safe Reliable, the burner is equipped with a multi-stage gas emergency cut-off and discharge device, the combustion chamber is a six-sided heavy furnace wall with explosion-proof doors, the heating furnace gas combustion is safe and reliable, and the accident loss is small; the invention has high thermal efficiency, and biomass gas production Low calorific value, less radiative heat transfer and more convection heat transfer, the structure of radiation section + multi-stage convection section is adopted to ensure that the smoke temperature is less than or equal to the inlet temperature of the heat carrier + 20°C.

最后应说明的几点是:首先,在本发明的描述中,需要说明的是,除非另有规定和限定,术语“安装”、“相连”、“连接”应做广义理解,可以是机械连接或电连接,也可以是两个元件内部的连通,可以是直接相连,“上”、“下”、“左”、“右”等仅用于表示相对位置关系,当被描述对象的绝对位置改变,则相对位置关系可能发生改变;The last points that should be noted are: First, in the description of the present invention, it should be noted that, unless otherwise specified and limited, the terms "installation", "connection" and "connection" should be understood in a broad sense, and may be mechanical connection. or electrical connection, or internal communication between two components, or direct connection, "up", "down", "left", "right", etc. are only used to indicate relative positional relationship, when the absolute position of the object being described changes, the relative positional relationship may change;

其次:本发明公开实施例附图中,只涉及到与本公开实施例涉及到的结构,其他结构可参考通常设计,在不冲突情况下,本发明同一实施例及不同实施例可以相互组合;Secondly: in the drawings of the disclosed embodiments of the present invention, only the structures involved in the embodiments of the present disclosure are involved, other structures may refer to the general design, and the same embodiment and different embodiments of the present invention can be combined with each other under the condition of no conflict;

最后:以上所述仅为本发明的优选实施例而已,并不用于限制本发明,凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。Finally: the above is only the preferred embodiment of the present invention, and is not intended to limit the present invention. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the present invention. within the scope of protection.

Claims (7)

1. The utility model provides a fire heat carrier heating furnace that living beings gas, includes furnace body (1) and combustion chamber (2), combustion chamber (2) set up in furnace body (1) below, its characterized in that: one side of combustion chamber (2) is provided with combustor (3), furnace body (1) inside one side bottom of keeping away from combustor (3) is installed and is radiated section coil pipe (4), the upper end of radiating section coil pipe (4) is connected with ceiling pipe (5), one side that the inside of furnace body (1) is located radiation section coil pipe (4) and ceiling pipe (5) is provided with the convection section, the outer end of furnace body (1) is provided with import header (6), the one end of import header (6) sets up in furnace body (1) internal connection has convection section header (7), the upper end of furnace body (1) is provided with export header (8) and outlet flue (13).
2. The heat carrier heating furnace for biomass-fired gas production according to claim 1, characterized in that: the combustor interface is arranged on the side wall of the combustion chamber (2), the combustor (3) is installed at the combustor interface, the combustor (3) is a high-temperature low-nitrogen gas combustor, and a multi-stage gas emergency cut-off device and a discharge device are arranged on the combustor (3).
3. The heat carrier heating furnace for biomass-fired gas production according to claim 1, characterized in that: the combustion chamber (2) adopts negative pressure combustion, and the biomass gasification device directly sends the gas to the combustion chamber (2) for combustion after gas making, without an intermediate storage tank and pressurization.
4. The heat carrier heating furnace for biomass-fired gas production according to claim 1, characterized in that: the periphery and the lower part of the combustion chamber (3) are all heat insulation furnace walls, and the upper part of the combustion chamber (3) is provided with a furnace arch and a throat.
5. The heat carrier heating furnace for biomass-fired gas production according to claim 1, characterized in that: the convection section comprises a first convection section (9), a second convection section (10), a third convection section (11) and a fourth convection section (12), one end of the radiant section coil pipe (4) at one end of the first convection section (9) is connected, and one end of the fourth convection section (12) is connected with the convection section header pipe (7).
6. The heat carrier heating furnace for biomass-fired gas production according to claim 5, characterized in that: the first convection section (9), the second convection section (10), the third convection section (11) and the fourth convection section (12) adopt a multi-stage parallel or series structure, and the space between the pipe pieces of each stage of convection section is gradually reduced along with the flowing direction of flue gas.
7. The heat carrier heating furnace for biomass-fired gas production according to claim 5, characterized in that: one end of the ceiling pipe (5) far away from the radiant section coil pipe (4) is connected with an outlet header pipe (8).
CN202210889488.2A 2022-07-27 2022-07-27 A heat carrier heating furnace for burning biomass to make gas Pending CN115234899A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116558115A (en) * 2023-05-11 2023-08-08 常州能源设备股份有限公司 High-safety large biomass gas-fired organic heat carrier furnace

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CN202328775U (en) * 2011-12-06 2012-07-11 常州能源设备总厂有限公司 Square-box-shaped heat carrier heating furnace
CN206755585U (en) * 2017-04-28 2017-12-15 常州能源设备总厂有限公司 Organic heat carrier furnace
CN212585212U (en) * 2020-05-20 2021-02-23 无锡景锡锅炉有限公司 Biomass gasification furnace
CN214949795U (en) * 2021-04-20 2021-11-30 常州能源设备总厂有限公司 Large organic heat carrier furnace with spliced furnace body structure
CN217875821U (en) * 2022-07-27 2022-11-22 常州能源设备总厂有限公司 Heat carrier heating furnace for producing gas by burning biomass

Patent Citations (5)

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Publication number Priority date Publication date Assignee Title
CN202328775U (en) * 2011-12-06 2012-07-11 常州能源设备总厂有限公司 Square-box-shaped heat carrier heating furnace
CN206755585U (en) * 2017-04-28 2017-12-15 常州能源设备总厂有限公司 Organic heat carrier furnace
CN212585212U (en) * 2020-05-20 2021-02-23 无锡景锡锅炉有限公司 Biomass gasification furnace
CN214949795U (en) * 2021-04-20 2021-11-30 常州能源设备总厂有限公司 Large organic heat carrier furnace with spliced furnace body structure
CN217875821U (en) * 2022-07-27 2022-11-22 常州能源设备总厂有限公司 Heat carrier heating furnace for producing gas by burning biomass

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116558115A (en) * 2023-05-11 2023-08-08 常州能源设备股份有限公司 High-safety large biomass gas-fired organic heat carrier furnace

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Application publication date: 20221025