JP2017032266A - Heat transfer pipe of fluidized bed boiler - Google Patents

Heat transfer pipe of fluidized bed boiler Download PDF

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JP2017032266A
JP2017032266A JP2016119335A JP2016119335A JP2017032266A JP 2017032266 A JP2017032266 A JP 2017032266A JP 2016119335 A JP2016119335 A JP 2016119335A JP 2016119335 A JP2016119335 A JP 2016119335A JP 2017032266 A JP2017032266 A JP 2017032266A
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protector
fluidized bed
heat transfer
transfer tube
bed boiler
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JP6691834B2 (en
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洋和 梶原
Hirokazu Kajiwara
洋和 梶原
栄司 石川
Eiji Ishikawa
栄司 石川
恭久 本田
Yasuhisa Honda
恭久 本田
野口 学
Manabu Noguchi
学 野口
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Ebara Environmental Plant Co Ltd
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Ebara Environmental Plant Co Ltd
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Priority to EP16180608.8A priority Critical patent/EP3124862B1/en
Priority to KR1020160094550A priority patent/KR102522883B1/en
Priority to CN201610605304.XA priority patent/CN106402850B/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • F28F19/002Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using inserts or attachments
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23CMETHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00Fluidised bed combustion apparatus
    • F23C10/18Details; Accessories
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24HFLUID HEATERS, e.g. WATER OR AIR HEATERS, HAVING HEAT-GENERATING MEANS, e.g. HEAT PUMPS, IN GENERAL
    • F24H1/00Water heaters, e.g. boilers, continuous-flow heaters or water-storage heaters
    • F24H1/22Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating
    • F24H1/40Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes
    • F24H1/41Water heaters other than continuous-flow or water-storage heaters, e.g. water heaters for central heating with water tube or tubes in serpentine form
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D2021/0019Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
    • F28D2021/0024Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for combustion apparatus, e.g. for boilers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2275/00Fastening; Joining
    • F28F2275/08Fastening; Joining by clamping or clipping
    • F28F2275/085Fastening; Joining by clamping or clipping with snap connection
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste

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

Abstract

PROBLEM TO BE SOLVED: To provide a heat transfer pipe of a fluidized bed boiler including a protector having sufficient durability under a corrosive wear environment while lowering initial costs by preventing a complicated structure, considering maintenance performance such as attachment and replacement, and reducing risks of cracking and deformation.SOLUTION: In a heat transfer pipe 1 used in a fluidized bed of a fluidized bed boiler, the heat transfer pipe 1 is composed of a water pipe 2 in which a fluid flows, a thin protector 4 and a thick protector 3 made of casting, disposed at an outer peripheral side of the water pipe 2 and protecting the water pipe 2, a heat insulating layer 6 disposed between the water pipe 2 and the thin protector 4, and a fixing jig 5. The fixing fig 5 is fixed to the thick protector 3, and the thin protector 4 disposed at the outer peripheral side of the water pipe 2 is pressed by the fixing jig 5.SELECTED DRAWING: Figure 3

Description

本発明は、廃棄物やRDF(ごみ固形化燃料)、バイオマスなどの燃料を燃焼させて燃焼熱を回収する流動層ボイラの流動層内で用いる伝熱管に関する。   The present invention relates to a heat transfer tube used in a fluidized bed of a fluidized bed boiler that recovers combustion heat by burning fuel such as waste, RDF (garbage solidified fuel), and biomass.

近年、化石燃料の価格高騰や地球温暖化問題等への対応といった観点から、エネルギー資源の活用が求められている。このなかで、サーマルリサイクルの一翼を担う廃棄物やRDF、バイオマスなどの燃料を燃焼させる発電システムの重要性が増加している。この発電システムには、流動層ボイラを用いて廃棄物やRDF、バイオマスなどの燃料を燃焼した際に発生する熱エネルギーを伝熱管で回収する方式がある。この方式では、流動層ボイラで廃棄物やRDF、バイオマスなどの燃料を燃焼させる際に、燃料中に起因する塩化物により激しい腐食環境が形成される場合がある。ここに流動媒体による摩耗が加わることにより伝熱管のプロテクタに著しい減肉が引き起こされ、プロテクタ自身の寿命が短くなり、頻繁なメンテナンスが必要となる。   In recent years, utilization of energy resources has been demanded from the standpoint of dealing with rising prices of fossil fuels and global warming problems. In this situation, the importance of power generation systems that burn fuels such as waste, RDF, and biomass that play a role in thermal recycling is increasing. In this power generation system, there is a method in which heat energy generated when a fuel such as waste, RDF, or biomass is burned using a fluidized bed boiler is recovered by a heat transfer tube. In this method, when a fuel such as waste, RDF, or biomass is burned in a fluidized bed boiler, a severe corrosive environment may be formed by chloride derived from the fuel. The wear caused by the fluidized medium causes a significant reduction in the thickness of the protector of the heat transfer tube, shortens the life of the protector itself, and requires frequent maintenance.

プロテクタの延命化対策としては、表面硬化層の形成による耐摩耗性の改善や、特許文献1に開示されているようにプロテクタの表面にスタッドを設けることにより粒子の衝突速度を緩和させる方法が知られている。
また、特許文献2においては、プロテクタと伝熱管の間に空隙を設けることによりプロテクタ表面温度を上昇させ、表面に酸化皮膜を形成させ、耐摩耗性を向上させている。プロテクタにSUSなどのステンレス系材質を用いる場合には温度上昇により酸化皮膜が生じ、耐摩耗性が向上し、減肉量が減少することは、特許文献3でも報告されている。
As measures for prolonging the life of the protector, there are known methods for improving wear resistance by forming a hardened surface layer and for reducing the collision speed of particles by providing studs on the surface of the protector as disclosed in Patent Document 1. It has been.
Moreover, in patent document 2, a protector surface temperature is raised by providing a space | gap between a protector and a heat exchanger tube, an oxide film is formed in the surface, and abrasion resistance is improved. It is also reported in Patent Document 3 that when a stainless steel material such as SUS is used for the protector, an oxide film is formed due to temperature rise, wear resistance is improved, and the amount of thinning is reduced.

一方、特許文献4においては、プロテクタと伝熱管の間にアルミ溶射層を設け、アルミが溶融することにより密着度を向上させプロテクタの表面温度を下げて腐食を抑制する方法が提案されている。
また、プロテクタに十分な減肉代を設けることも寿命を確保するための対策の一つである。板材やパイプ材では厚みが限定され、さらに厚板の加工にコストが掛かるため、鋳物を使用することが一般的である。
On the other hand, Patent Document 4 proposes a method in which an aluminum sprayed layer is provided between the protector and the heat transfer tube, and the aluminum is melted to improve adhesion and lower the surface temperature of the protector to suppress corrosion.
Also, providing the protector with a sufficient thickness reduction is one of the measures for ensuring the life. Since the thickness of the plate material and the pipe material is limited, and the processing of the thick plate is costly, it is common to use a casting.

特開2004−19965号公報Japanese Patent Laid-Open No. 2004-19965 特開平5−18504号公報JP-A-5-18504 特開平8−226601号公報JP-A-8-226601 実開平5−25101号公報Japanese Utility Model Publication No. 5-25101

上述したように、プロテクタの延命化対策として表面硬化層を形成する場合、特別な処理が必要になり、プロテクタのコストアップに繋がる。また単純なエロージョンに対しては効果的であるが、腐食が関与する環境での効果は限定的である。表面スタッドなどによる摩耗条件の緩和は、摩耗および腐食摩耗の双方の現象に対し効果的である。しかし、構造が複雑になるため、プロテクタのコストアップと共にメンテナンスが複雑になる。   As described above, when the surface hardened layer is formed as a measure for prolonging the life of the protector, special treatment is required, leading to an increase in the cost of the protector. It is effective against simple erosion, but has limited effects in environments where corrosion is involved. Relaxation of wear conditions such as by surface studs is effective for both wear and corrosion wear phenomena. However, since the structure becomes complicated, the cost of the protector increases and the maintenance becomes complicated.

長寿命化対策の厚肉化については、鋳物は厚肉化が容易で低コストであるが、材質的に溶接が難しい場合がある。また、現場での溶接作業自体が難しい場合もあり、メンテナンス性の観点からは現地での溶接作業が少ないことが望まれる。例えば、プロテクタにより伝熱管全面を保護する場合、溶接箇所が増え作業負荷が高くなり、設置・交換作業性の悪化に繋がる。特に、伝熱管の全周を保護する必要がある場合、プロテクタ個数が増えるため、複雑なプロテクタはコストアップのみならず作業効率の低下を招く。また、厚肉プロテクタは重量が嵩む点からも作業性が低下する。さらに、厚肉のプロテクタを組み合わせて嵌め合い構造とした場合、運転中にプロテクタと伝熱管の間に流動媒体が侵入し、冷却時に過大な応力が発生しプロテクタが割れるリスクが生じる。   With regard to increasing the wall thickness as a measure for prolonging the service life, castings can be easily increased in thickness and cost reduced, but there are cases where welding is difficult due to the material. In addition, the welding work at the site itself may be difficult, and it is desired that the welding work at the site is small from the viewpoint of maintainability. For example, when the entire surface of the heat transfer tube is protected by a protector, the number of welding points is increased and the work load is increased, leading to deterioration in installation / exchange workability. In particular, when it is necessary to protect the entire circumference of the heat transfer tube, the number of protectors increases, so a complicated protector not only increases costs but also decreases work efficiency. In addition, the workability of the thick protector is also reduced from the viewpoint of increasing the weight. Further, when a fitting structure is formed by combining thick protectors, a fluid medium enters between the protector and the heat transfer tube during operation, and there is a risk that excessive stress is generated during cooling and the protector breaks.

耐摩耗の観点からプロテクタの温度を上げることは有効とされているが、プロテクタと伝熱管の間に空隙を設けると、運転中の膨張した空隙に流動媒体が入り込み、停止時に収縮することにより過大な応力が発生し、プロテクタの割れや変形などのリスクが生じる。また一方で耐食の観点からは、プロテクタ表面温度を下げることが提案されており、腐食と摩耗の双方が関与する条件での適切な条件については適切な手段が見出されていない。   It is effective to raise the temperature of the protector from the viewpoint of wear resistance. However, if a gap is provided between the protector and the heat transfer tube, the fluidized medium will enter the expanded gap during operation and shrink at the time of stoppage. Stresses occur and risks such as breakage and deformation of the protector occur. On the other hand, from the viewpoint of corrosion resistance, it has been proposed to lower the protector surface temperature, and no appropriate means has been found for appropriate conditions in which both corrosion and wear are involved.

本発明は、これらの課題に対しなされたもので、複雑な構造を避けることでイニシャルコストを下げ、かつ取付けや交換などのメンテナンス性を考慮し、かつ割れや変形のリスクを低減し、腐食摩耗環境で十分な耐久性を有するプロテクタを備えた流動層ボイラの伝熱管を提供することを目的とする。   The present invention has been made for these problems, and avoids complicated structures, lowers initial cost, considers maintainability such as installation and replacement, reduces the risk of cracking and deformation, and corrosive wear. An object of the present invention is to provide a heat transfer tube of a fluidized bed boiler provided with a protector having sufficient durability in the environment.

上述の目的を達成するため、本発明者らは、プロテクタの延命化を図る手段について研究を重ねたものであり、以下に研究過程を説明する。
構造の複雑化を避けてプロテクタを延命化させる手段として厚肉化が有効な手段であり、しかも低コストでプロテクタの構造を製造するための最良の手段は鋳造である。溶接を避けるため厚肉プロテクタと固定治具を嵌め合い構造で固定させた伝熱管を用いて試験を行った。しかし、水管とプロテクタおよび固定治具の間に生じた隙間に流動媒体が侵入し、熱収縮時に過大な応力が発生しプロテクタが割れるトラブルが頻発するに到った。そのため固定治具を極力小さくし発生する応力を低減させることで割れを防止した。また固定治具を小さくしたことで重量が減り、現場での作業性も向上した。
In order to achieve the above-described object, the present inventors have conducted research on means for prolonging the life of the protector, and the research process will be described below.
Thickening is an effective means for extending the life of the protector while avoiding the complexity of the structure, and casting is the best means for producing the structure of the protector at a low cost. In order to avoid welding, the test was conducted using a heat transfer tube in which a thick protector and a fixing jig were fitted and fixed in a structure. However, the fluid medium entered the gap formed between the water pipe, the protector, and the fixing jig, and excessive stress was generated at the time of thermal contraction, resulting in frequent trouble that the protector was broken. Therefore, cracks were prevented by reducing the generated stress by making the fixing jig as small as possible. Also, by reducing the size of the fixture, the weight was reduced and the workability on site was improved.

一方で薄肉プロテクタの課題は耐久性である。従来技術では耐摩耗の観点からは表面温度を上げることが提案されており、耐食の観点からは温度を下げることが提案されている。
この矛盾に対し、本発明者らは実機で1年間プロテクタとしてSUS310とSCH13を使用し、材質的にはSUS310の方が耐食性に優れるにもかかわらず、SUS310が激しい減肉を引起すことを見出した。SUS310は薄板で伝熱管に密着していたが、鋳物であるSCH13は密着度が劣り且つ厚肉で、表面温度を比較するとSUS310の方が数百度低い状況で運転されていた。つまり腐食摩耗環境で減肉を抑制するには金属の温度を上げることが有効であることを見出した。この知見に基づいて薄肉プロテクタと水管の間に断熱層を設けることで薄肉プロテクタの表面温度を上昇させ、減肉を抑制できることを見出した。なお、薄肉プロテクタの応力による損傷を防ぐため、薄肉プロテクタと水管の間に流動媒体が侵入することを防ぐことが望ましい。
On the other hand, the problem with thin protectors is durability. In the prior art, it has been proposed to increase the surface temperature from the viewpoint of wear resistance, and it has been proposed to decrease the temperature from the viewpoint of corrosion resistance.
In response to this contradiction, the present inventors have used SUS310 and SCH13 as protectors for one year on actual machines, and found that SUS310 causes severe thinning, although SUS310 is superior in corrosion resistance in terms of material. It was. SUS310 was a thin plate and was in close contact with the heat transfer tube, but SCH13, which was a casting, was inferior in adhesion and thick, and was operated in a situation where SUS310 was several hundred degrees lower when compared with the surface temperature. In other words, it has been found that raising the metal temperature is effective in suppressing thinning in a corrosive wear environment. Based on this knowledge, it discovered that the surface temperature of a thin protector can be raised by providing a heat insulation layer between a thin protector and a water pipe, and thickness reduction can be suppressed. In order to prevent damage to the thin protector due to stress, it is desirable to prevent the fluid medium from entering between the thin protector and the water pipe.

本発明は、以上の知見とそれに基づく試験により完成し、腐食摩耗環境で伝熱管の全周を保護する以下の手段を提供する。
本発明の流動層ボイラの伝熱管は、流動層ボイラの流動層内で用いる伝熱管において、前記伝熱管は、内部を流体が流れる水管と、前記水管の外周側に設けられ前記水管を保護するための薄肉プロテクタおよび鋳物製の厚肉プロテクタと、前記水管と前記薄肉プロテクタの間に設けられる断熱層と、固定治具とから構成され、前記固定治具を前記厚肉プロテクタに固定し、前記固定治具で前記水管の外周側に設けられた前記薄肉プロテクタを押さえるようにしたことを特徴とする。厚肉プロテクタの厚さは10mm〜50mmであり、薄肉プロテクタの厚さは2mm〜6mmである。
The present invention is completed by the above knowledge and tests based thereon, and provides the following means for protecting the entire circumference of the heat transfer tube in a corrosive wear environment.
A heat transfer tube of a fluidized bed boiler according to the present invention is a heat transfer tube used in a fluidized bed of a fluidized bed boiler, wherein the heat transfer tube is provided on the outer peripheral side of the water tube and a water tube through which a fluid flows, and protects the water tube. A thin-wall protector for casting and a thick-wall protector made of casting, a heat insulating layer provided between the water tube and the thin-wall protector, and a fixing jig, and fixing the fixing jig to the thick-wall protector, The thin protector provided on the outer peripheral side of the water pipe is pressed by a fixing jig. The thickness of the thick protector is 10 mm to 50 mm, and the thickness of the thin protector is 2 mm to 6 mm.

本発明の好ましい態様は、前記固定治具を前記厚肉プロテクタに嵌め合い構造で固定したことを特徴とする。
本発明の好ましい態様は、前記嵌め合い構造は、前記固定治具および前記厚肉プロテクタの一方に設けられたガイド溝と、前記固定治具および前記厚肉プロテクタの他方に設けられた突起部とからなることを特徴とする。
本発明の好ましい態様は、前記断熱層への流動媒体侵入に対する防止構造を有することを特徴とする。
In a preferred aspect of the present invention, the fixing jig is fitted to the thick protector and fixed with a structure.
In a preferred aspect of the present invention, the fitting structure includes a guide groove provided on one of the fixing jig and the thick protector, and a protrusion provided on the other of the fixing jig and the thick protector. It is characterized by comprising.
A preferred embodiment of the present invention is characterized by having a structure for preventing a fluid medium from entering the heat insulating layer.

本発明の好ましい態様は、前記薄肉プロテクタを二重構造とし、前記薄肉プロテクタの間に前記断熱層を設けたことを特徴とする。
本発明の好ましい態様は、前記断熱層は、断熱ペーパーからなることを特徴とする。
本発明の好ましい態様は、前記固定治具は鋳物製であることを特徴とする。
本発明の好ましい態様は、前記固定治具でカバーされる前記薄肉プロテクタの部分の面積は、前記薄肉プロテクタの外周面の面積の50%以下であることを特徴とする。
In a preferred aspect of the present invention, the thin protector has a double structure, and the heat insulating layer is provided between the thin protectors.
In a preferred aspect of the present invention, the heat insulating layer is made of heat insulating paper.
In a preferred aspect of the present invention, the fixing jig is made of a casting.
In a preferred aspect of the present invention, the area of the thin protector covered by the fixing jig is 50% or less of the area of the outer peripheral surface of the thin protector.

本発明の好ましい態様は、前記薄肉プロテクタにフィンを設けたことを特徴とする。
本発明の流動層ボイラは、燃料を流動層内で燃焼させ、燃焼熱を伝熱管で回収する流動層ボイラにおいて、前記伝熱管は、上記伝熱管であることを特徴とする。
本発明の好ましい態様は、前記流動層ボイラは、燃料を燃焼させるための燃焼室と、層内伝熱管が配置され燃焼熱を回収する熱回収室とを備え、熱回収室の流動化空気の空気量をu/umf=2.0〜4.0にして流動媒体が前記燃焼室と前記熱回収室とを循環する内部循環流動層ボイラであることを特徴とする。
In a preferred aspect of the present invention, the thin protector is provided with fins.
The fluidized bed boiler of the present invention is a fluidized bed boiler that burns fuel in a fluidized bed and collects combustion heat with a heat transfer tube, wherein the heat transfer tube is the heat transfer tube.
In a preferred aspect of the present invention, the fluidized bed boiler includes a combustion chamber for burning fuel, and a heat recovery chamber in which an in-layer heat transfer tube is disposed to recover combustion heat, and the fluidized air in the heat recovery chamber The fluidized medium is an internal circulating fluidized bed boiler that circulates between the combustion chamber and the heat recovery chamber with an air amount of u 0 / u mf = 2.0 to 4.0.

本発明により、溶接作業が最小化されたため取付け・交換作業が容易で、低コストで厚肉製品が製造可能な鋳物で製作することによりコストを抑え、かつ腐食摩耗による損傷を低減させた長寿命のプロテクタを備えた流動層ボイラの伝熱管を提供することが可能である。   The present invention minimizes welding and minimizes damage by reducing wear and damage due to corrosion and wear by making castings that can produce thick-walled products at a low cost. It is possible to provide a heat transfer tube of a fluidized bed boiler equipped with a protector.

図1は、本発明に係る伝熱管を備えた流動層ボイラの一実施形態を示す模式的断面図である。FIG. 1 is a schematic cross-sectional view showing an embodiment of a fluidized bed boiler provided with a heat transfer tube according to the present invention. 図2は、本発明に係る伝熱管の斜視図である。FIG. 2 is a perspective view of a heat transfer tube according to the present invention. 図3は、図2のIII-III線断面図である。3 is a cross-sectional view taken along line III-III in FIG. 図4は、図2および図3に示す伝熱管の組立手順を示す分解斜視図である。FIG. 4 is an exploded perspective view showing an assembly procedure of the heat transfer tube shown in FIGS. 2 and 3.

以下、本発明に係る流動層ボイラの伝熱管の実施形態を図1乃至図4を参照して説明する。図1乃至図4において、同一または相当する構成要素には、同一の符号を付して重複した説明を省略する。
図1は、本発明に係る伝熱管を備えた流動層ボイラの一実施形態を示す模式的断面図である。図1に示すように、流動層ボイラ11は、略四角筒形状の炉本体12を備えており、炉本体12内は左右一対の仕切壁13,13によって、中央部にある1つの燃焼室14と、両側部にある2つの熱回収室15,15とに分割されている。燃焼室14内には、廃棄物やRDF等の燃料を熱反応させる流動床20が形成され、流動床20は炉床底板30によって支えられている。炉本体12内に設置された炉床底板30は、中央が高く、両側縁に向かうにつれ徐々に低くなった山形状をなしている。炉床底板30には、流動化ガスとしての流動化空気を炉内に噴出するための多数の散気ノズルが配置されている。各熱回収室15内には流動床23が形成され、この流動床23は炉床底板31によって支えられている。炉床底板31には、流動化ガスとしての流動化空気を炉内に噴出するための散気ノズルが配置されている。
Hereinafter, an embodiment of a heat transfer tube of a fluidized bed boiler according to the present invention will be described with reference to FIGS. 1 to 4. 1 to 4, the same or corresponding components are denoted by the same reference numerals, and redundant description is omitted.
FIG. 1 is a schematic cross-sectional view showing an embodiment of a fluidized bed boiler provided with a heat transfer tube according to the present invention. As shown in FIG. 1, the fluidized bed boiler 11 includes a furnace body 12 having a substantially rectangular tube shape, and the inside of the furnace body 12 is a single combustion chamber 14 in the center by a pair of left and right partition walls 13 and 13. And two heat recovery chambers 15 on both sides. In the combustion chamber 14, a fluidized bed 20 that thermally reacts fuel such as waste and RDF is formed, and the fluidized bed 20 is supported by a hearth bottom plate 30. The hearth bottom plate 30 installed in the furnace body 12 has a mountain shape in which the center is high and gradually lowers toward both side edges. A large number of diffuser nozzles for ejecting fluidized air as fluidized gas into the furnace are disposed on the bottom floor plate 30. A fluidized bed 23 is formed in each heat recovery chamber 15, and the fluidized bed 23 is supported by a hearth bottom plate 31. A diffuser nozzle for ejecting fluidized air as fluidized gas into the furnace is disposed on the hearth bottom plate 31.

図1に示すように、山形状の炉床底板30の下方には4つの空気箱32,32,33,33が形成されており、これら空気箱32,32,33,33には炉外から流動化空気が供給されるようになっている。調節弁(図示せず)の開度を調節して空気箱32,32,33,33に供給する空気流量を調節することにより、中央部の2つの空気箱32,32の上方の散気ノズルからは、実質的に小さな流動化速度を与えるように流動化空気を噴出し、両側部の2つの空気箱33,33の上方の散気ノズルからは、実質的に大きな流動化速度を与えるように流動化空気を噴出する。その結果、炉床底板30の中央部の上方に流動媒体が比較的ゆっくりした速度で上方から下方に移動する移動層21が形成され、炉床底板30の両側部の上方に流動媒体が下方から上方に移動する流動層22が形成される。したがって、流動床20の下部では流動媒体が移動層21から流動層22へ、流動床20の上部では流動媒体が流動層22から移動層21へ移動することで、移動層21と流動層22との間を流動媒体が循環する循環流が左右に形成される。各仕切壁13の傾斜部は、上昇する流動媒体が炉本体12の内部側に反転しやすくなるデフレクタとして機能する。   As shown in FIG. 1, four air boxes 32, 32, 33, and 33 are formed below the mountain-shaped hearth bottom plate 30, and these air boxes 32, 32, 33, and 33 are formed from outside the furnace. Fluidized air is supplied. By adjusting the opening of a control valve (not shown) to adjust the flow rate of air supplied to the air boxes 32, 32, 33, 33, an air diffuser nozzle above the two air boxes 32, 32 in the central portion. From the above, the fluidized air is ejected so as to give a substantially small fluidization speed, and the air diffuser nozzles above the two air boxes 33 on both sides are given a substantially large fluidization speed. Fluidized air is jetted out. As a result, a moving bed 21 in which the fluid medium moves from the upper side to the lower side at a relatively slow speed is formed above the center portion of the hearth bottom plate 30, and the fluid medium flows from the lower side above both sides of the hearth bottom plate 30. A fluidized bed 22 moving upward is formed. Accordingly, the fluidized medium moves from the moving bed 21 to the fluidized bed 22 at the lower part of the fluidized bed 20, and the fluidized medium moves from the fluidized bed 22 to the moving bed 21 at the upper part of the fluidized bed 20. A circulation flow in which the fluid medium circulates between the left and right is formed. The inclined portion of each partition wall 13 functions as a deflector that makes it easier for the rising fluid medium to reverse to the inside of the furnace body 12.

図1に示すように構成された内部循環流動層ボイラ11において、燃料は投入口(図示せず)から移動層21に供給される。このとき、調節弁の開度を調節して移動層21に供給する流動化空気の空気量が流動層22に供給する流動化空気の空気量よりも小さくなるように調節している。本実施の形態では移動層21に供給する流動化空気の空気量を2〜3u/umf、流動層22に供給する流動化空気の空気量を4〜6u/umfとしている。ここで、uは、空塔速度であり、umfは最低流動化空塔速度である。 In the internal circulating fluidized bed boiler 11 configured as shown in FIG. 1, fuel is supplied to the moving bed 21 from an inlet (not shown). At this time, the amount of fluidized air supplied to the moving bed 21 is adjusted so as to be smaller than the amount of fluidized air supplied to the fluidized bed 22 by adjusting the opening of the control valve. In the present embodiment, the amount of fluidized air supplied to the moving bed 21 is 2 to 3 u 0 / u mf , and the amount of fluidized air supplied to the fluidized bed 22 is 4 to 6 u 0 / u mf . Here, u 0 is the superficial velocity, and u mf is the minimum fluidized superficial velocity.

移動層21に供給された燃料は流動媒体に飲み込まれて流動媒体と共に下方に移動する。このとき、流動媒体の熱によって燃料の熱分解が行われて、燃料中の可燃分から可燃ガスが発生して、脆い熱分解残渣となる。熱分解残渣は、典型的には、不燃物及び熱分解によって脆くなった未燃物(チャー)を含んでいる。移動層21で生成される熱分解残渣は、流動媒体と共に、炉床底板30に至ると、傾斜した炉床底板30に沿って流動層22に向かう。流動層22に至った熱分解残渣は、激しく流動する流動媒体と接触し未燃物が不燃物から剥離し、未燃物が剥離して残った不燃物は、一部の流動媒体と共に不燃物排出口17から排出される。   The fuel supplied to the moving bed 21 is swallowed by the fluid medium and moves downward together with the fluid medium. At this time, the fuel is thermally decomposed by the heat of the fluidized medium, and combustible gas is generated from the combustible component in the fuel, resulting in a brittle thermal decomposition residue. The pyrolysis residue typically includes incombustible material and unburned material (char) that has become brittle by thermal decomposition. When the pyrolysis residue produced in the moving bed 21 reaches the hearth bottom plate 30 together with the fluidized medium, it goes toward the fluidized bed 22 along the inclined hearth bottom plate 30. The pyrolysis residue that has reached the fluidized bed 22 comes into contact with the fluid medium that flows violently, the unburned material is peeled off from the incombustible material, and the unburned material left after the unburned material is peeled off together with some of the fluidized medium. It is discharged from the discharge port 17.

一方、不燃物から剥離した未燃物は、流動化空気が供給されることに伴って流動する流動媒体と共に上方に移動する。このとき、未燃物は、供給された流動化空気によって燃焼が行われ、流動媒体を加熱しつつ燃焼ガスを発生し、気体に搬送される程度の微細な未燃物及び灰分の粒子となる。流動層22の上部に至った高温の流動媒体の一部は、移動層21に流入する。流動媒体は、流動層22において、移動層21に流動したときに燃料の熱分解を適切に行うことができる温度に上昇させられる。移動層21に流入した流動媒体は、再び供給された燃料を受け入れて、上述の移動層21及び流動層22における熱反応を繰り返す。移動層21の温度は700〜900℃に維持され、流動層22の温度は700〜900℃に維持される。   On the other hand, the unburned material peeled from the incombustible material moves upward together with the fluid medium that flows as fluidized air is supplied. At this time, the unburned material is combusted by the supplied fluidized air, generates a combustion gas while heating the fluidized medium, and becomes fine unburned material and ash particles that are conveyed to the gas. . A part of the high-temperature fluid medium that reaches the top of the fluidized bed 22 flows into the moving bed 21. The fluid medium is raised in the fluidized bed 22 to a temperature at which the fuel can be thermally decomposed appropriately when it flows into the moving bed 21. The fluid medium flowing into the moving bed 21 receives the supplied fuel again and repeats the thermal reaction in the moving bed 21 and the fluidized bed 22 described above. The temperature of the moving bed 21 is maintained at 700 to 900 ° C, and the temperature of the fluidized bed 22 is maintained at 700 to 900 ° C.

また、流動層22の上部の高温の流動媒体の一部は、仕切壁13の上部を越えて熱回収室15に入り込む。燃焼室14と熱回収室15との間には、熱回収室15を囲むように多数のスクリーン水管2が略垂直方向に設置されており、流動媒体はこれらスクリーン水管2の間を通って熱回収室15に入り込むようになっている。熱回収室15に入り込んだ流動媒体は、上方から下方に移動する流動床23を形成する。熱回収室15の炉床底板31は炉本体12の内壁側から燃焼室側に向かって下方に傾斜しており、熱回収室15の下部には開口部18が設けられ、熱回収室15に入り込んだ流動媒体は、流動床23を形成しつつ沈降し、開口部18から燃焼室14へ循環する。熱回収室15に入り込む流動媒体の温度は、700〜900℃であるが、熱回収室15の流動床23内には層内伝熱管16が配設されており、高温になった流動媒体は下方に移動しつつ層内伝熱管16と接触し、層内伝熱管16内の流体(缶水)は流動媒体と熱交換を行うことにより流動媒体から熱を回収する。流動床23の炉床底板31の散気ノズルから噴出させる流動化空気の空気量を2〜4u/umfに制御することにより、層内伝熱管16の熱回収量を制御することができる。燃焼室14へ循環した流動媒体は、流動層22に合流し、流動層22の流動媒体とともに上昇し、一部の流動媒体は、再び熱回収室15に入り込み、上述の層内伝熱管16内の流体との熱交換を繰り返す。 A part of the high-temperature fluid medium above the fluidized bed 22 enters the heat recovery chamber 15 beyond the upper part of the partition wall 13. A large number of screen water tubes 2 are installed between the combustion chamber 14 and the heat recovery chamber 15 in a substantially vertical direction so as to surround the heat recovery chamber 15. It enters the recovery chamber 15. The fluid medium that has entered the heat recovery chamber 15 forms a fluidized bed 23 that moves downward from above. The hearth bottom plate 31 of the heat recovery chamber 15 is inclined downward from the inner wall side of the furnace body 12 toward the combustion chamber side, and an opening 18 is provided in the lower portion of the heat recovery chamber 15. The fluid medium that has entered sinks while forming the fluidized bed 23 and circulates from the opening 18 to the combustion chamber 14. The temperature of the fluid medium that enters the heat recovery chamber 15 is 700 to 900 ° C., but the in-layer heat transfer pipe 16 is disposed in the fluidized bed 23 of the heat recovery chamber 15, The fluid (can water) in the in-layer heat transfer tube 16 recovers heat from the flowing medium by exchanging heat with the flowing medium. By controlling the amount of fluidized air ejected from the diffuser nozzle of the hearth bottom plate 31 of the fluidized bed 23 to 2-4 u 0 / u mf , the heat recovery amount of the in-layer heat transfer tube 16 can be controlled. . The fluidized medium circulated to the combustion chamber 14 joins the fluidized bed 22 and rises together with the fluidized medium in the fluidized bed 22, and a part of the fluidized medium enters the heat recovery chamber 15 again, and the inside of the above-described in-layer heat transfer tube 16. Repeat heat exchange with the fluid.

本発明に係る伝熱管を、図1に示す流動層ボイラ11のスクリーン水管2に適用した実施形態について、図2乃至図4を参照して説明する。
図2は本発明に係る伝熱管の斜視図であり、図3は図2のIII-III線断面図である。図4は、図2および図3に示す伝熱管の組み立て手順を示す分解斜視図である。
図2および図3に示すように、伝熱管1は、内部に流体(缶水)が流れる円筒状の水管(スクリーン水管)2と、水管2の円周面の一部を囲むように設けられた断面コ字状の厚肉プロテクタ3と、厚肉プロテクタ3の反対側において水管2の円周面を囲むように設けられた断面U字状の薄肉プロテクタ4と、薄肉プロテクタ4を上から押さえた状態で厚肉プロテクタ3に嵌め合いで固定されている断面U字状の固定治具5とを備えている。すなわち、水管2の全周は厚肉プロテクタ3と薄肉プロテクタ4により囲まれて保護されている。厚肉プロテクタ3の厚さは10mm〜50mmであり、薄肉プロテクタ4の厚さは2mm〜6mmである。
An embodiment in which the heat transfer tube according to the present invention is applied to the screen water tube 2 of the fluidized bed boiler 11 shown in FIG. 1 will be described with reference to FIGS.
2 is a perspective view of a heat transfer tube according to the present invention, and FIG. 3 is a cross-sectional view taken along line III-III in FIG. FIG. 4 is an exploded perspective view showing a procedure for assembling the heat transfer tubes shown in FIGS. 2 and 3.
As shown in FIGS. 2 and 3, the heat transfer tube 1 is provided so as to surround a cylindrical water tube (screen water tube) 2 through which a fluid (canned water) flows and a part of the circumferential surface of the water tube 2. The U-shaped thick protector 3, the U-shaped thin protector 4 provided to surround the circumferential surface of the water pipe 2 on the opposite side of the thick protector 3, and the thin protector 4 are pressed from above. And a fixing jig 5 having a U-shaped cross section that is fitted and fixed to the thick-wall protector 3. That is, the entire circumference of the water pipe 2 is surrounded and protected by the thick protector 3 and the thin protector 4. The thickness of the thick protector 3 is 10 mm to 50 mm, and the thickness of the thin protector 4 is 2 mm to 6 mm.

燃焼室14と熱回収室15を仕切るスクリーン水管2は、腐食環境および摩耗条件とも燃焼室側が厳しくなる。より厳しい燃焼室側は鋳物で作製した厚肉プロテクタ3で全面を保護した。一方、条件が比較的マイルドな熱回収室側は薄肉プロテクタ4で保護し、固定治具5は薄肉プロテクタ4を押さえるために必要最小限の大きさとしている。これにより厚肉プロテクタ3と固定治具5の嵌め合い部で発生する応力を抑制し、厚肉プロテクタ3の割れを防ぐことができる。また併せて全体重量が低減され、メンテナンス性も向上する。また作業性効率の向上の観点から、より軽くするために一つの固定治具5の大きさを小さくし、固定治具5は全体で2段構造になっている。   The screen water pipe 2 that divides the combustion chamber 14 and the heat recovery chamber 15 becomes severe on the combustion chamber side in both corrosive environment and wear conditions. The more severe combustion chamber side was protected with a thick protector 3 made of casting. On the other hand, the relatively mild heat recovery chamber side is protected by the thin protector 4, and the fixing jig 5 has a minimum size necessary for holding the thin protector 4. Thereby, the stress which generate | occur | produces in the fitting part of the thick protector 3 and the fixing jig 5 can be suppressed, and the crack of the thick protector 3 can be prevented. In addition, the overall weight is reduced and the maintainability is improved. From the viewpoint of improving work efficiency, the size of one fixing jig 5 is reduced in order to make it lighter, and the fixing jig 5 has a two-stage structure as a whole.

本発明においては、厚肉プロテクタ3および固定治具5は、SCS13,SCS14,SCS18,SCH13,SCH21,SCH22等のステンレス系鋳物もしくは耐熱鋳鋼とし、薄肉プロテクタ4はSUS304,SUS310,SUS316等のステンレス鋼やSS400等の鉄鋼で形成する。本実施形態においては、製造コストおよび取り付けの容易性を考慮し、厚肉プロテクタ3は鋳物で、薄肉プロテクタ4はSUS310ステンレス鋼の板材で製造している。   In the present invention, the thick protector 3 and the fixing jig 5 are stainless steel castings such as SCS13, SCS14, SCS18, SCH13, SCH21, and SCH22 or heat-resistant cast steel, and the thin protector 4 is stainless steel such as SUS304, SUS310, and SUS316. And steel such as SS400. In the present embodiment, in consideration of manufacturing cost and ease of attachment, the thick protector 3 is manufactured from a casting, and the thin protector 4 is manufactured from a plate material of SUS310 stainless steel.

本発明者らは、流動層内の雰囲気に曝される薄肉プロテクタ4とスクリーン水管2が直接接触すると金属表面温度が低下し雰囲気に曝される部分で腐食摩耗減肉が促進されることを発見した為、薄肉プロテクタ4とスクリーン水管2の間に断熱層を設けて過度の冷却を防止するようにしている。薄肉プロテクタ4と水管2との間に設ける断熱層は、断熱材や断熱キャスタブル等で形成し、断熱層に流動媒体が流入するのを防ぐ。この場合、断熱材の形状は特に限定されず、例えばペーパー状、繊維状、粉末状、バルク状であってもよい。本実施形態では、断熱層として断熱ペーパー6を採用している。断熱層を空気層とする場合には、断熱層への流動媒体の流入を防ぐために、厚肉プロテクタ3や薄肉プロテクタ4の上方に鋳物や鉄鋼等で形成した笠を設けてもよい。断熱層の厚みは0.25mm以上が望ましい。薄肉プロテクタ4を二重構造とし、二重構造の薄肉プロテクタと薄肉プロテクタの間に断熱層を設けてもよい。薄肉プロテクタ4の表面温度を上昇させるために薄肉プロテクタにフィンを設けてもよい。   The present inventors have found that when the thin protector 4 exposed to the atmosphere in the fluidized bed and the screen water pipe 2 are in direct contact, the metal surface temperature is lowered and corrosion wear reduction is promoted in the exposed portion. For this reason, an insulating layer is provided between the thin protector 4 and the screen water pipe 2 to prevent excessive cooling. The heat insulating layer provided between the thin protector 4 and the water pipe 2 is formed of a heat insulating material, a heat insulating castable or the like, and prevents the flowing medium from flowing into the heat insulating layer. In this case, the shape of the heat insulating material is not particularly limited, and may be, for example, paper, fiber, powder, or bulk. In this embodiment, the heat insulation paper 6 is employ | adopted as a heat insulation layer. When the heat insulating layer is an air layer, a cap formed of cast metal or steel may be provided above the thick protector 3 or the thin protector 4 in order to prevent the flowing medium from flowing into the heat insulating layer. The thickness of the heat insulating layer is desirably 0.25 mm or more. The thin protector 4 may have a double structure, and a heat insulating layer may be provided between the thin protector having the double structure and the thin protector. In order to increase the surface temperature of the thin protector 4, fins may be provided on the thin protector.

本発明においては、厚肉プロテクタ3と固定治具5とを嵌め合い構造で固定することにより、溶接せずに簡便に取り付けることを可能にした。厚肉プロテクタ3もしくは固定治具5の一方にガイド溝を設け、このガイド溝に固定治具5もしくは厚肉プロテクタ3の突起部を嵌め込む構造とする。ただし、ガイド溝を設けた部分に熱応力が発生するため、割れ防止の観点より、面積が大きい厚肉プロテクタ側にガイド溝を取り付けることが好ましい。本実施形態では、断面コ字状の厚肉プロテクタ3は、両側部の内面にガイド溝3g,3gを備えており、断面U字状の固定治具5は、開口側の両側部に突起部5a,5aを備えている。そして、固定治具5の突起部5a,5aが厚肉プロテクタ3のガイド溝3g,3gに嵌合することにより、固定治具5は厚肉プロテクタ3に固定されるようになっている。なお、固定治具5及び厚肉プロテクタ3に切り穴を設け、ボルト・ナットで固定してもよい。   In the present invention, the thick protector 3 and the fixing jig 5 are fitted and fixed with a fitting structure, so that they can be easily attached without welding. A guide groove is provided in one of the thick protector 3 or the fixing jig 5, and the protruding portion of the fixing jig 5 or the thick protector 3 is fitted into the guide groove. However, since thermal stress is generated in the portion where the guide groove is provided, it is preferable to attach the guide groove to the thick protector side having a large area from the viewpoint of preventing cracking. In this embodiment, the thick protector 3 having a U-shaped cross section is provided with guide grooves 3g, 3g on the inner surfaces of both side portions, and the fixing jig 5 having a U-shaped cross section is a protrusion on both side portions on the opening side. 5a, 5a. The fixing jig 5 is fixed to the thick protector 3 by fitting the projections 5 a and 5 a of the fixing jig 5 into the guide grooves 3 g and 3 g of the thick protector 3. Note that a cut hole may be provided in the fixing jig 5 and the thick protector 3 and fixed with bolts and nuts.

固定治具5が大きいと、プロテクタ3,4を含めた全体が重くなり取扱いが困難になると共に、ガイド溝部に発生する熱応力が大きくなるため、小さい方が望ましく、固定治具5により薄肉プロテクタ4がカバーされる部分の面積は、薄肉プロテクタ4の外周面の面積の50%以下、望ましくは30%以下とする。なお、固定治具5により薄肉プロテクタ4がカバーされる部分の面積は、薄肉プロテクタ4の外周面の面積の20%以上とする。固定治具5は1段でも複数段でも構わない。メンテナンス時には薄肉プロテクタあるいは断熱層など必要な部分のみ交換することができる。   If the fixing jig 5 is large, the entire body including the protectors 3 and 4 becomes heavy and difficult to handle, and the thermal stress generated in the guide groove portion increases, so a smaller one is desirable. The area of the portion covered with 4 is 50% or less, preferably 30% or less of the area of the outer peripheral surface of the thin protector 4. The area of the portion where the thin protector 4 is covered by the fixing jig 5 is 20% or more of the area of the outer peripheral surface of the thin protector 4. The fixing jig 5 may be one stage or a plurality of stages. During maintenance, only necessary parts such as thin protectors or heat insulation layers can be replaced.

次に、プロテクタのスクリーン水管2への取り付け手順について、図4を参照して説明する。図4に示すように、最初に断熱ペーパー6をスクリーン水管2に巻きつけ、その後、厚肉プロテクタ3と薄肉プロテクタ4とを組み合わせ、最後に厚肉プロテクタ3に設けられたガイド溝3gに固定治具5の突起部5aを嵌合することにより、厚肉プロテクタ3に固定治具5を取り付ける。   Next, a procedure for attaching the protector to the screen water pipe 2 will be described with reference to FIG. As shown in FIG. 4, the heat insulating paper 6 is first wound around the screen water tube 2, and then the thick protector 3 and the thin protector 4 are combined, and finally fixed to the guide groove 3 g provided in the thick protector 3. The fixing jig 5 is attached to the thick protector 3 by fitting the protrusion 5 a of the tool 5.

図2乃至図4に示す本発明の構造、および薄肉プロテクタの代わりに厚肉プロテクタと同じ大きさの固定治具を用いた場合(比較例1)、薄肉プロテクタと水管の間に断熱層を設けなかった場合(比較例2)を並べて実機で評価した。実証結果のまとめを表1に記す。
表1に示すように、割れについて、本発明品および比較例2では問題は無かったが、比較例1では割れが見られた。減肉については、何れも厚肉プロテクタおよび固定治具については減肉率が僅かで、十分な寿命が見込まれた。一方、薄肉プロテクタについては、断熱層を設けない比較例2では固定治具がない環境に露出した部分で激しい減肉が見られた。また、本発明品では、プロテクタは十分な肉厚が残存し、プロテクタとしての十分な寿命を有することが確認できた。メンテナンス性については、比較例2が最も容易で、本発明品は、比較例2に比べ断熱ペーパーを取付ける作業の分だけ工数が増加するが、大きな手間ではない。一方、比較例1は重量のある厚肉プロテクタと固定治具を組み合わせるため、作業性が悪く、さらに運転中に噛み込んだ流動媒体により取り外しにも手間が掛かる結果となった。
以上のとおり、本発明品は総合的に判断し、耐久性やメンテナンス性に優れていることを実証した。

Figure 2017032266
When the structure of the present invention shown in FIGS. 2 to 4 and a fixing jig having the same size as the thick protector is used instead of the thin protector (Comparative Example 1), a heat insulating layer is provided between the thin protector and the water pipe. When there was not (Comparative Example 2), it evaluated by the actual machine. A summary of the verification results is shown in Table 1.
As shown in Table 1, although there was no problem with the product of the present invention and Comparative Example 2, cracks were seen in Comparative Example 1. As for the thickness reduction, the thickness reduction rate was small for the thick protector and the fixing jig, and a sufficient life was expected. On the other hand, with regard to the thin protector, in Comparative Example 2 in which the heat insulating layer was not provided, severe thinning was observed in a portion exposed to an environment without a fixing jig. In the product of the present invention, it was confirmed that the protector had a sufficient thickness and had a sufficient life as a protector. As for maintainability, Comparative Example 2 is the easiest, and the product of the present invention increases the man-hour for the work of attaching the heat insulating paper as compared with Comparative Example 2, but it is not a great effort. On the other hand, in Comparative Example 1, since the heavy thick protector and the fixing jig were combined, the workability was poor, and further, it took time to remove the fluid medium that was bitten during operation.
As described above, the product of the present invention was comprehensively judged and proved to be excellent in durability and maintainability.
Figure 2017032266

これまで本発明の実施形態について説明したが、本発明は上述の実施形態に限定されず、その技術思想の範囲内において、種々の異なる形態で実施されてよいことは勿論である。   Although the embodiment of the present invention has been described so far, the present invention is not limited to the above-described embodiment, and it is needless to say that the present invention may be implemented in various different forms within the scope of the technical idea.

1 伝熱管
2 スクリーン水管
3 厚肉プロテクタ
3g ガイド溝
4 薄肉プロテクタ
5 固定治具
5a 突起部
6 断熱ペーパー
11 流動層ボイラ
12 炉本体
13 仕切壁
14 燃焼室
15 熱回収室
16 層内伝熱管
17 不燃物排出口
18 開口部
20 流動床
21 移動層
22 流動層
23 流動床
30 炉床底板
31 炉床底板
32 空気箱
33 空気箱
DESCRIPTION OF SYMBOLS 1 Heat transfer tube 2 Screen water tube 3 Thick protector 3g Guide groove 4 Thin protector 5 Fixing jig 5a Protrusion part 6 Heat insulation paper 11 Fluidized bed boiler 12 Furnace main body 13 Partition wall 14 Combustion chamber 15 Heat recovery chamber 16 In-layer heat transfer tube 17 Noncombustible Material outlet 18 Opening 20 Fluidized bed 21 Moving bed 22 Fluidized bed 23 Fluidized bed 30 Furnace bottom plate 31 Furnace bottom plate 32 Air box 33 Air box

Claims (11)

流動層ボイラの流動層内で用いる伝熱管において、
前記伝熱管は、内部を流体が流れる水管と、前記水管の外周側に設けられ前記水管を保護するための薄肉プロテクタおよび鋳物製の厚肉プロテクタと、前記水管と前記薄肉プロテクタの間に設けられる断熱層と、固定治具とから構成され、
前記固定治具を前記厚肉プロテクタに固定し、前記固定治具で前記水管の外周側に設けられた前記薄肉プロテクタを押さえるようにしたことを特徴とする流動層ボイラの伝熱管。
In heat transfer tubes used in the fluidized bed of a fluidized bed boiler,
The heat transfer pipe is provided between a water pipe through which a fluid flows, a thin protector provided on the outer peripheral side of the water pipe to protect the water pipe and a cast-type thick protector, and the water pipe and the thin protector. It consists of a heat insulation layer and a fixing jig,
A heat transfer tube of a fluidized bed boiler, wherein the fixing jig is fixed to the thick protector, and the thin protector provided on the outer peripheral side of the water tube is pressed by the fixing jig.
前記固定治具を前記厚肉プロテクタに嵌め合い構造で固定したことを特徴とする請求項1に記載の流動層ボイラの伝熱管。   The heat transfer tube of a fluidized bed boiler according to claim 1, wherein the fixing jig is fitted to the thick protector and fixed with a structure. 前記嵌め合い構造は、前記固定治具および前記厚肉プロテクタの一方に設けられたガイド溝と、前記固定治具および前記厚肉プロテクタの他方に設けられた突起部とからなることを特徴とする請求項2に記載の流動層ボイラの伝熱管。   The fitting structure includes a guide groove provided on one of the fixing jig and the thick protector, and a protrusion provided on the other of the fixing jig and the thick protector. A heat transfer tube of a fluidized bed boiler according to claim 2. 前記断熱層への流動媒体侵入に対する防止構造を有することを特徴とする請求項1乃至3のいずれか一項に記載の流動層ボイラの伝熱管。   The heat transfer tube of a fluidized bed boiler according to any one of claims 1 to 3, further comprising a structure for preventing fluid medium from entering the heat insulating layer. 前記薄肉プロテクタを二重構造とし、前記薄肉プロテクタの間に前記断熱層を設けたことを特徴とする請求項1乃至4のいずれか一項に記載の流動層ボイラの伝熱管。   The heat transfer tube of a fluidized bed boiler according to any one of claims 1 to 4, wherein the thin protector has a double structure, and the heat insulating layer is provided between the thin protectors. 前記断熱層は、断熱ペーパーからなることを特徴とする請求項1乃至5のいずれか一項に記載の流動層ボイラの伝熱管。   The heat transfer tube of a fluidized bed boiler according to any one of claims 1 to 5, wherein the heat insulating layer is made of heat insulating paper. 前記固定治具は鋳物製であることを特徴とする請求項1乃至6のいずれか一項に記載の流動層ボイラの伝熱管。   The heat transfer tube of a fluidized bed boiler according to any one of claims 1 to 6, wherein the fixing jig is made of a casting. 前記固定治具でカバーされる前記薄肉プロテクタの部分の面積は、前記薄肉プロテクタの外周面の面積の50%以下であることを特徴とする請求項1乃至7のいずれか一項に記載の流動層ボイラの伝熱管。   8. The flow according to claim 1, wherein an area of the portion of the thin protector covered by the fixing jig is 50% or less of an area of an outer peripheral surface of the thin protector. Layer boiler heat transfer tube. 前記薄肉プロテクタにフィンを設けたことを特徴とする請求項1乃至8のいずれか一項に記載の流動層ボイラの伝熱管。   The heat transfer tube of a fluidized bed boiler according to any one of claims 1 to 8, wherein fins are provided on the thin protector. 燃料を流動層内で燃焼させ、燃焼熱を伝熱管で回収する流動層ボイラにおいて、
前記伝熱管は、請求項1乃至9のいずれか一項に記載の伝熱管であることを特徴とする流動層ボイラ。
In a fluidized bed boiler that burns fuel in a fluidized bed and collects the heat of combustion with a heat transfer tube,
The fluidized bed boiler, wherein the heat transfer tube is the heat transfer tube according to any one of claims 1 to 9.
前記流動層ボイラは、燃料を燃焼させるための燃焼室と、層内伝熱管が配置され燃焼熱を回収する熱回収室とを備え、熱回収室の流動化空気の空気量をu/umf=2.0〜4.0にして流動媒体が前記燃焼室と前記熱回収室とを循環する内部循環流動層ボイラであることを特徴とする請求項10に記載の流動層ボイラ。 The fluidized bed boiler includes a combustion chamber for burning fuel, and a heat recovery chamber in which an in-layer heat transfer tube is arranged to recover combustion heat, and the amount of fluidized air in the heat recovery chamber is u 0 / u. The fluidized bed boiler according to claim 10, wherein the fluidized medium is an internal circulation fluidized bed boiler that circulates between the combustion chamber and the heat recovery chamber with mf = 2.0 to 4.0.
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