JP6393438B1 - Method of spraying irregular refractories for coke oven carbonization chamber and spraying material used therefor - Google Patents

Method of spraying irregular refractories for coke oven carbonization chamber and spraying material used therefor Download PDF

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JP6393438B1
JP6393438B1 JP2018056030A JP2018056030A JP6393438B1 JP 6393438 B1 JP6393438 B1 JP 6393438B1 JP 2018056030 A JP2018056030 A JP 2018056030A JP 2018056030 A JP2018056030 A JP 2018056030A JP 6393438 B1 JP6393438 B1 JP 6393438B1
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本田 和寛
和寛 本田
和典 関
和典 関
義隆 石井
義隆 石井
山田 貴史
貴史 山田
統一 白曼
統一 白曼
翼 中道
翼 中道
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Krosaki Harima Corp
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Abstract

【課題】材料供給機から先端吹付けノズルに至る材料搬送管に注水器を設け、この注水器から材料搬送管内を搬送される吹付け材料に施工水を注水するコークス炉炭化室用不定形耐火物の吹付け施工方法において、その吹付け施工の安定性を向上させるとともに均し作業の作業性を向上させる。【解決手段】材料供給機1から先端吹付けノズル4に至る材料搬送管5に注水器7を設け、この注水器から材料搬送管内を搬送される吹付け材料に施工水を注水するコークス炉炭化室用不定形耐火物の吹付け施工方法において、注水器7に導入される施工水を搬送するための施工水搬送用ガスの流量(Nm3/min)と、吹付け材料を搬送するための吹付け材料搬送用ガスの流量(Nm3/min)との比(施工水搬送用ガスの流量/吹付け材料搬送用ガスの流量)を0.07以上2以下とし、かつ、吹付け材料の圧縮度を15%以上32%以下とする。【選択図】図1[PROBLEMS] To provide a water injection device in a material conveyance pipe from a material supply machine to a tip spray nozzle, and to inject the construction water into the spray material conveyed in the material conveyance pipe from this water injection machine, for an irregular fireproofing for a coke oven carbonization chamber. In the method of spraying objects, the stability of the spraying work is improved and the workability of the leveling work is improved. A coke oven carbonization is provided in which a water injector 7 is provided in a material transport pipe 5 extending from a material supply machine 1 to a tip spray nozzle 4 and construction water is poured into the spray material transported from the water feeder into the material transport pipe. In the method of spraying room-specific refractories, the flow rate (Nm3 / min) of the construction water transport gas for transporting the construction water introduced into the water injector 7 and the spray for transporting the spray material. The ratio (flow rate of construction water transfer gas / flow rate of spray material transfer gas) to 0.07 to 2 with the flow rate of the transfer material transfer gas (Nm3 / min), and the compressibility of the spray material Between 15% and 32%. [Selection] Figure 1

Description

本発明は、コークス炉炭化室用の不定形耐火物の吹付け施工方法、及びそれに使用する吹付け材料に関する。   The present invention relates to a method for spraying an irregular refractory for a coke oven carbonization chamber, and a spray material used therefor.

まず、一般的な不定形耐火物の吹付け施工方法について説明すると、その吹付け施工方法は湿式施工方法と乾式施工方法とに大別できる。
湿式施工方法は施工水を予め材料へ添加して混練しスラリー状とした吹付け材料を圧送して先端吹付けノズル部において急結剤等を添加して吹付ける工法である。他方、乾式施工方法は吹付け材料を乾燥状態でガス搬送し、先端吹付けノズル部で施工水を注水して吹付ける工法である。
First, a general spraying method for an irregular refractory will be described. The spraying method can be roughly classified into a wet method and a dry method.
The wet construction method is a construction method in which construction water is added to a material in advance and kneaded to form a slurry-like spraying material, and a quick setting agent or the like is added and sprayed at a tip spray nozzle portion. On the other hand, the dry construction method is a construction method in which the spray material is transported by gas in a dry state, and the construction water is injected and sprayed at the tip spray nozzle portion.

湿式施工方法は乾式施工方法に比べて付着性に優れた緻密質の耐火物の吹付け施工体を形成することができ、施工に際しての発塵量が少ない等の効果がある。反面、吹付けに際して混練装置やスラリー圧送装置が必要で、その上、装置の構造が複雑で高価であり、また、吹付け作業後はスラリー状の吹付け材料が混練装置や搬送ホース内に付着し、その洗浄作業に手間取るという欠点がある。   The wet construction method is capable of forming a dense refractory spray construction body having better adhesion than the dry construction method, and has the effect of reducing the amount of dust generated during construction. On the other hand, a kneading device and a slurry pumping device are required for spraying, and the structure of the device is complicated and expensive, and after spraying, slurry-like spraying material adheres to the kneading device and the conveyance hose. However, there is a drawback that it takes time for the cleaning operation.

これに対して、乾式施工方法は、基本的には乾燥状態でガス搬送された吹付け材料に先端吹付けノズル部で、施工水を注水するのみであるので、吹付け装置は簡単で作業性に優れているが、吹付け材料に水分(施工水)が十分に混合されない状態での吹付けであるため、吹付けに際して、粉塵が多く発生し、吹付け施工体の耐火物組織も不均一となる傾向があり、付着率、接着強度及び耐食性も劣ったものとなる。湿式施工方法と比較すると混練効果が低く施工水量が多いため緻密な吹付け施工体が得られにくいという欠点もある。   On the other hand, in the dry construction method, the spraying device is basically simple and workable because the construction water is simply injected into the spraying material that has been transported in a dry state by the tip spray nozzle. Although the spraying is performed in a state where water (construction water) is not sufficiently mixed with the spray material, a lot of dust is generated during spraying, and the refractory structure of the sprayed body is uneven. The adhesion rate, adhesive strength and corrosion resistance are also inferior. Compared with the wet construction method, there is also a drawback that it is difficult to obtain a dense spray construction body because the kneading effect is low and the amount of construction water is large.

そこで、乾式施工方法の改良として、材料供給機から先端吹付けノズルに至る材料搬送管に2つの注水器を設け、それぞれの注水器から平均100μm以下の微粒化水を圧縮空気と共に注水する吹付け施工方法が知られている(例えば、特許文献1参照)。
しかしながら、本発明者らがこの吹付け施工方法による吹付け施工を数多く実施したところ、吹付け材料の吐出量が変動したり、吹付け材料と施工水とが分離したりする現象が散見され、吹付け施工の安定性に改善の余地があることがわかった。
Therefore, as an improvement of the dry construction method, two water injectors are provided in the material transport pipe from the material supply machine to the tip spray nozzle, and spraying that sprays atomized water with an average of 100 μm or less together with compressed air from each water injector A construction method is known (see, for example, Patent Document 1).
However, when the present inventors carried out a lot of spraying construction by this spraying construction method, the discharge amount of the spraying material fluctuates or a phenomenon that the spraying material and the construction water are separated is occasionally seen. It was found that there was room for improvement in the stability of spray construction.

一方、コークス炉炭化室の損傷箇所への不定形耐火物の吹付け施工においては、1人が吹付けを行い、もう1人が吹付け材料を平滑化するための均し作業を行う。そのため、コークス炉炭化室用不定形耐火物の吹付け施工方法においては、吹付けた吹付け材料の均しやすさも求められる。   On the other hand, in the spraying construction of the irregular refractory to the damaged part of the coke oven carbonization chamber, one person sprays and the other person performs the leveling work to smooth the spray material. For this reason, in the method of spraying an irregular refractory for a coke oven carbonization chamber, it is also required that the sprayed spray material is even.

特許第4377913号公報Japanese Patent No. 4377913

本発明が解決しようとする課題は、材料供給機から先端吹付けノズルに至る材料搬送管に注水器を設け、この注水器から材料搬送管内を搬送される吹付け材料に施工水を注水するコークス炉炭化室用不定形耐火物の吹付け施工方法において、その吹付け施工の安定性を向上させるとともに均し作業の作業性を向上させることにある。   The problem to be solved by the present invention is to provide a water injection device in a material conveyance pipe from the material supply machine to the tip spray nozzle, and to inject the construction water into the spraying material conveyed in the material conveyance pipe from this water injection device In the method of spraying an amorphous refractory for a furnace carbonization chamber, it is to improve the stability of the spraying work and improve the workability of the leveling work.

本発明者らは、まず吹付け施工の安定性を向上させるには吹付け材料に対する施工水の混水性と吹付け材料の搬送性を向上させることが重要と考え試験を重ねたところ、注水器に導入される施工水を搬送するための施工水搬送用ガスの流量(Nm/min)と、吹付け材料を搬送するための吹付け材料搬送用ガスの流量(Nm/min)との比、及び吹付け材料の圧縮度が、前述の混水性及び搬送性を向上させ、ひいては吹付け施工の安定性を向上させるための重要なパラメータであることを知見した。さらに、均し作業の作業性を向上させる観点から試験を重ねたところ、この均し作業の作業性を向上させる観点からも吹付け材料の圧縮度が重要なパラメータであることを知見し、本発明を完成するに至った。 The inventors of the present invention first conducted a test of a water injector when it was considered important to improve the water mixing of the construction water with respect to the spray material and the transportability of the spray material in order to improve the stability of the spray construction. flow construction water carrier gas for transporting the construction water introduced into the (Nm 3 / min), the spraying material conveying gas for conveying the spraying material flow (Nm 3 / min) and the It has been found that the ratio and the degree of compression of the spray material are important parameters for improving the above-mentioned water-mixing and transportability and thus improving the stability of the spraying construction. Furthermore, when tests were repeated from the viewpoint of improving the workability of the leveling work, it was found that the compressibility of the spray material was an important parameter from the viewpoint of improving the workability of the leveling work. The invention has been completed.

すなわち、本発明の一観点によれば次の吹付け施工方法が提供される。
材料供給機から先端吹付けノズルに至る材料搬送管に注水器を1つのみ設け、この注水器から材料搬送管内を搬送される吹付け材料に注水するコークス炉炭化室用不定形耐火物の吹付け施工方法であって、
前記注水器に導入される施工水を搬送するための施工水搬送用ガスの流量(Nm/min)と、吹付け材料を搬送するための吹付け材料搬送用ガスの流量(Nm/min)との比(施工水搬送用ガスの流量/吹付け材料搬送用ガスの流量)が0.07以上2以下であり、かつ、前記吹付け材料の圧縮度が15%以上32%以下である、コークス炉炭化室用不定形耐火物の吹付け施工方法。
That is, according to one aspect of the present invention, the following spray construction method is provided.
Only one water injector is installed in the material transport pipe from the material feeder to the tip spray nozzle, and the spraying of the amorphous refractory for the coke oven carbonization chamber that injects water into the spray material transported through the material transport pipe from this water injector. It is an installation method,
The flow rate of the construction water carrier gas for transporting the construction water introduced into the water injector and (Nm 3 / min), the spraying material conveying gas for conveying the spraying material flow (Nm 3 / min ) (Flow rate of construction water carrying gas / flow rate of blowing material carrying gas) is 0.07 or more and 2 or less, and the compressibility of the blowing material is 15% or more and 32% or less. , A method for spraying amorphous refractories for coke oven carbonization chambers.

また、本発明の他の観点によれば、本発明のコークス炉炭化室用不定形耐火物の吹付け施工方法に使用する吹付け材料であって、圧縮度が15%以上32%以下である吹付け材料が提供される。   Moreover, according to the other viewpoint of this invention, it is a spraying material used for the spraying construction method of the amorphous refractory for coke oven carbonization chambers of this invention, Comprising: A compressibility is 15% or more and 32% or less. Spray material is provided.

本発明によれば、吹付け施工の際、吹付け材料に対する施工水の混水性と吹付け材料の搬送性が向上し、その結果、吹付け施工の安定性が向上する。また、本発明によれば、均し作業の作業性も向上する。   According to the present invention, at the time of spraying construction, the mixed water of the construction water with respect to the spraying material and the transportability of the spraying material are improved, and as a result, the stability of the spraying construction is improved. Further, according to the present invention, the workability of leveling work is also improved.

本発明の吹付け施工方法を実施するための吹付け装置の一例を示す概念図。The conceptual diagram which shows an example of the spraying apparatus for enforcing the spraying construction method of this invention. 実施例及び比較例で吹付け対象としたシャモットれんがの概念的な断面図。The conceptual sectional drawing of the chamotte brick made into the spray object by an Example and a comparative example.

まず、本発明の吹付け施工方法を実施するための吹付け装置の一例を、図1を参照しつつ説明する。   First, an example of the spray apparatus for implementing the spray construction method of this invention is demonstrated, referring FIG.

図1において、1は吹付け材料2が収納された材料供給機を示す。材料供給機1は、一般に不定形耐火物の吹付け装置に使用されているもので定量吐出できるものであれば、ロテクターガン、リードガン、野上セメントガン等のいかなるタイプのものでも問題なく使用することができる。   In FIG. 1, reference numeral 1 denotes a material supply machine in which a spray material 2 is stored. As long as the material supply machine 1 is generally used in spraying devices for irregular refractories and can discharge a fixed amount, any type of material such as a protector gun, a lead gun, or a field cement gun can be used without any problem. it can.

この材料供給機1内の吹付け材料2は、材料供給機1内に供給される圧縮空気等のガスによって内圧が調整され、下端に設けられたモータMによって駆動するテーブルフィーダー3によって、材料供給機1から先端吹付けノズル4に至る材料搬送管5に供給される。   The spray material 2 in the material supply machine 1 is supplied with a material by a table feeder 3 that is driven by a motor M provided at the lower end, the internal pressure of which is adjusted by a gas such as compressed air supplied into the material supply machine 1. It is supplied to the material conveying pipe 5 from the machine 1 to the tip spray nozzle 4.

材料搬送管5にはテーブルフィーダー3の吹付け材料搬送用ガス導入管6を通して吹付け材料搬送用ガスが供給され、材料供給機1からの吹付け材料2を材料搬送管5の先端吹付けノズル4からコークス炉炭化室Aに吹付け施工する。   The material conveying pipe 5 is supplied with the blowing material conveying gas through the blowing material conveying gas introduction pipe 6 of the table feeder 3, and the blowing material 2 from the material supply machine 1 is supplied to the tip of the material conveying pipe 5. 4 is sprayed onto the coke oven carbonization chamber A.

この材料搬送管5には、先端吹付けノズル4の近傍に注水器7が1つのみ設けられている。コークス炉での吹付け施工は、作業者が先端吹付けノズル4を持って行う手作業が主流であるので、先端吹付けノズル4近傍の構造はシンプルかつ軽量である必要がある。このため、注水器の数は1つに限定している。   The material transport pipe 5 is provided with only one water injector 7 in the vicinity of the tip spray nozzle 4. The spraying work in the coke oven is mainly performed manually by the operator holding the tip spray nozzle 4, so the structure in the vicinity of the tip spray nozzle 4 needs to be simple and lightweight. For this reason, the number of water injectors is limited to one.

注水器7からは、材料搬送管5内を搬送される吹付け材料2に施工水が施工水搬送用ガスと共に供給される。注水器7の構成は特に限定されず、材料搬送管5内に施工水を施工水搬送用ガスと共に供給(注水)できるものであればよい。注水器7からは、施工水が施工水搬送用ガスと共に注水されるから、その施工水は、いわゆる噴霧水(微粒化水)となる。
注水器7を設ける位置は、先端吹付けノズル4先端から0.5m以上5m未満の範囲が好ましく、より好ましくは、0.5m以上3m未満である。なお、先端吹付けノズル4の長さは、概ね1m以上10m以下である。
From the water injector 7, the construction water is supplied together with the construction water transport gas to the spray material 2 transported through the material transport pipe 5. The configuration of the water injector 7 is not particularly limited as long as the construction water can be supplied (poured) into the material conveyance pipe 5 together with the construction water conveyance gas. Since the construction water is poured from the water injector 7 together with the construction water conveying gas, the construction water becomes so-called spray water (atomized water).
The position where the water injector 7 is provided is preferably in the range of 0.5 m or more and less than 5 m from the tip of the tip spray nozzle 4, more preferably 0.5 m or more and less than 3 m. The length of the tip spray nozzle 4 is approximately 1 m or more and 10 m or less.

本発明において使用する吹付け材料搬送用ガス及び施工水搬送用ガスは、典型的には空気(圧縮空気)であるが、例えば窒素(圧縮窒素)等の他のガスを使用することもできる。また、使用するガスの圧力は、概ね0.2MPa以上0.5MPa以下の範囲とすることができる。   The spray material conveying gas and the construction water conveying gas used in the present invention are typically air (compressed air), but other gases such as nitrogen (compressed nitrogen) can also be used. Moreover, the pressure of the gas to be used can be made into the range of about 0.2 MPa or more and 0.5 MPa or less.

次に、図1の吹付け装置を使用する形態により、本発明の吹付け施工方法を説明する。
本発明の吹付け施工方法の第一の特徴は、注水器7に導入される施工水を搬送するための施工水搬送用ガスの流量(Nm/min)と、吹付け材料を搬送するための吹付け材料搬送用ガスの流量(Nm/min)との比(施工水搬送用ガスの流量/吹付け材料搬送用ガスの流量)(以下「搬送用ガス流量比」という。)を0.07以上2以下とすることにある。この搬送用ガス流量比を0.07以上2以下とすることで、施工水の混水性と吹付け材料の搬送性が向上し、吹付け施工の安定性が向上する。
これに対して搬送用ガス流量比が0.07未満であると、吹付け材料搬送用ガスの流量が多いので、吹付け材料を搬送する材料搬送管5の中心部まで施工水が届かず、混水性が悪くなる。
一方、搬送用ガス流量比が2を超えると、施工水搬送用ガスの流量が多いので、吹付け材料搬送用ガスとの間で乱流が生じ、その結果、注水器7近傍での吹付け材料の付着や、さらにはその上流側の材料搬送管5にも吹付け材料の付着が生じ、吹付け材料の搬送性が低下する。
この搬送用ガス流量比は、0.1以上1以下であることが好ましい、
Next, the spraying construction method of the present invention will be described by using the spraying device of FIG.
The first feature of the spray construction method of the present invention is that the flow rate (Nm 3 / min) of the construction water transport gas for transporting the construction water introduced into the water injector 7 and the spray material are transported. The ratio of the flow rate of the spray material conveying gas (Nm 3 / min) (the flow rate of the construction water transfer gas / the flow rate of the spray material transfer gas) (hereinafter referred to as the “transport gas flow ratio”) is 0. 0.07 or more and 2 or less. By making this conveyance gas flow rate ratio 0.07 or more and 2 or less, the mixing water of construction water and the transportability of the spraying material are improved, and the stability of the spraying construction is improved.
On the other hand, if the transport gas flow ratio is less than 0.07, the flow rate of the spray material transport gas is large, so the construction water does not reach the center of the material transport pipe 5 that transports the spray material, Water mixing becomes worse.
On the other hand, if the transfer gas flow ratio exceeds 2, the flow rate of the construction water transfer gas is large, so that a turbulent flow occurs with the spray material transfer gas, and as a result, spraying in the vicinity of the water injector 7 The adhesion of the material and, further, the adhesion of the spray material also occurs on the material transport pipe 5 on the upstream side thereof, and the transportability of the spray material is deteriorated.
The transfer gas flow ratio is preferably 0.1 or more and 1 or less.

本発明の吹付け施工方法の第二の特徴は、吹付け材料として圧縮度が15%以上32%以下のものを使用することにある。言い換えれば、圧縮度が15%以上32%以下となるように粒度構成等を調整した吹付け材料を使用するということである。ここで圧縮度とは、次式により求められるものである。
圧縮度(%)=(密充填嵩密度−疎充填嵩密度)/密充填嵩密度×100
なお、詳細は後述するが、本発明で使用する吹付け材料は耐火原料粉末に加えて繊維を含有することがあるところ、繊維を含有する場合、圧縮度の評価(密充填嵩密度及び疎充填嵩密度の測定)は、繊維を除いた状態で実施するものとする。すなわち、吹付け材料が繊維を含有する場合、本発明でいう圧縮度とは、繊維を除いた吹付け材料について評価したものをいう。
The second feature of the spray construction method of the present invention is that a material having a degree of compression of 15% to 32% is used as the spray material. In other words, a spray material whose particle size configuration is adjusted so that the degree of compression is 15% or more and 32% or less is used. Here, the degree of compression is obtained by the following equation.
Compressibility (%) = (Densely packed bulk density−Roughly packed bulk density) / Densely packed bulk density × 100
In addition, although mentioned later for details, the spraying material used by this invention may contain a fiber in addition to a refractory raw material powder, When a fiber is contained, evaluation of a compressibility (dense filling bulk density and loose filling) The measurement of the bulk density is carried out in a state where the fibers are removed. That is, when a spray material contains a fiber, the compression degree said by this invention means what evaluated about the spray material except a fiber.

吹付け材料は施工水が添加されると、施工水と接触した粉末がスラリー化し粘性が高くなる傾向にあるところ、圧縮度が32%を超える吹付け材料は、静置状態でも多量の空気を含むため、施工水搬送用ガスの外力等により凝集しやすい。さらに、施工水の添加により部分的なスラリー粘性が高くなるため、ますます凝集が加速化し、施工水が均一に湿潤せず混水性が低下する。凝集が著しい場合は、吹付け材料が材料搬送管5内に固着して閉塞の要因となり、搬送性の低下を招くことになる。
一方、吹付け材料の圧縮度が15%未満であると、吹付けられた吹付け材料が低粘化(さらさら)しすぎるため均し作業の際、コークス炉炭化室から剥落しやすくなり、結果として均し作業の作業性が低下する。
この圧縮度は18%以上25%以下であることが好ましい。
When construction water is added to the spray material, the powder in contact with the construction water tends to become a slurry and become highly viscous. Since it contains, it is easy to aggregate by the external force etc. of the gas for construction water conveyance. Furthermore, since the partial slurry viscosity increases due to the addition of the construction water, the agglomeration is further accelerated and the construction water is not uniformly moistened, resulting in a decrease in water mixing. When aggregation is remarkable, spray material adheres in the material conveyance pipe | tube 5, becomes a cause of obstruction | occlusion, and causes a fall of conveyance property.
On the other hand, if the degree of compression of the spray material is less than 15%, the sprayed spray material is too low in viscosity (smooth), so it becomes easy to peel off from the coke oven carbonization chamber during the leveling operation. As a result, workability of the leveling work is reduced.
The degree of compression is preferably 18% or more and 25% or less.

本発明の吹付け施工方法において、施工水搬送用ガスの流量(Nm/min)と施工水量(m/min)との比(施工水搬送用ガスの流量/施工水量)(以下「ガス・施工水量比」という。)は100以上1000以下とすることが好ましい。このガス・施工水量比を100以上1000以下とすることで、施工水の混水性及び吹付け材料の搬送性、さらには吹付け施工の安定性が向上する。このガス・施工水量比は250以上800以下であることがさらに好ましい。 In the spray construction method of the present invention, the ratio of the flow rate (Nm 3 / min) of the construction water carrying gas to the construction water volume (m 3 / min) (the flow rate of the construction water carrying gas / the construction water volume) (hereinafter “gas” -It is preferable to set it as 100 or more and 1000 or less. By setting the gas / construction water amount ratio to 100 or more and 1000 or less, the water content of the construction water, the transportability of the spray material, and the stability of the spray construction are improved. The gas / construction water amount ratio is more preferably 250 or more and 800 or less.

本発明の吹付け施工方法において、吹付け材料の吐出量(kg/min)と搬送用ガスの合計流量(Nm/min)との比(吹付け材料の吐出量/搬送用ガスの合計流量)(以下「固気比」という。)は1以上20以下とすることが好ましい。この固気比を1以上20以下とすることで、施工水の混水性及び吹付け材料の搬送性、さらには吹付け施工の安定性が向上する。
なお、この固気比の計算に用いる「搬送用ガスの合計流量(Nm/min)」とは、吹付け材料搬送用ガス導入管6からの吹付け材料搬送用ガスの流量(Nm/min)と、注水器7からの施工水搬送用ガスの流量(Nm/min)の合計流量(Nm/min)のことをいう。
In the spray construction method of the present invention, the ratio of the discharge amount of spray material (kg / min) to the total flow rate of transport gas (Nm 3 / min) (discharge amount of spray material / total flow rate of transport gas) ) (Hereinafter referred to as “solid-gas ratio”) is preferably 1 or more and 20 or less. By setting this solid-gas ratio to 1 or more and 20 or less, the mixed water of the construction water, the transportability of the spray material, and the stability of the spray construction are improved.
Note that "total flow rate of carrier gas (Nm 3 / min)" used in this solid-gas ratio calculation, the spraying material conveying gas from spraying material carrier gas introduction pipe 6 a flow rate (Nm 3 / and min), refers to the flow rate of the construction water conveying gas from the water injector 7 (Nm 3 / min) total flow rate of (Nm 3 / min).

本発明の吹付け施工方法で使用する吹付け材料の粒度構成は、粒径0.5mm超4mm以下の粒子の含有量が20質量%以上50質量%以下、粒径45μm以下の粒子の含有量が10質量%以上40質量%以下であることが好ましい、これは均し作業の作業性を向上させるとともに、吹付け材料の充填性を向上させるためである。すなわち、コークス炉炭化室の損傷箇所には亀裂状の損傷(微亀裂)が存在することがあることから、その微亀裂への吹付け材料の充填されやすさも求められる。
粒径45μm以下の粒子の含有量が40質量%を超えると、吹付けられた吹付け材料の粘性が高くなり均し作業時の作業負荷が大きくなる。一方、粒径45μm以下の粒子の含有量が10質量%未満であると、均し作業時において微亀裂(数ミリレベルの幅)に吹付け材料が充填されにくくなる。
また、粒径0.5mm超4mm以下の粒子の含有量が50質量%を超えると、粘性が低下して均し作業の際、コークス炉炭化室から剥落しやすくなる。一方、粒径0.5mm超4mm以下の粒子の含有量が20質量%未満であると、粘性が高くなり均し作業時の作業負荷が大きくなる。
なお、この粒度構成は、吹付け材料の圧縮度を15%以上32%以下としやすい点からも好ましい。
ここで、本発明において、粒子の粒径がd超とは、その粒子が目開きdの篩上に残る粒度であることを意味し、粒子の粒径がd以下とは、その粒子が目開きdの篩を通過する粒度であることを意味する。
The particle size composition of the spray material used in the spray construction method of the present invention is that the content of particles having a particle size of more than 0.5 mm and not more than 4 mm is 20% by mass to 50% by mass, and the content of particles having a particle size of 45 μm or less. Is preferably not less than 10% by mass and not more than 40% by mass, in order to improve the workability of the leveling operation and to improve the filling property of the spray material. That is, since crack-like damage (microcracks) may exist at the damaged portion of the coke oven carbonization chamber, the ease of filling the spray material into the microcracks is also required.
When the content of particles having a particle diameter of 45 μm or less exceeds 40% by mass, the viscosity of the sprayed material becomes high and the work load during the leveling work increases. On the other hand, when the content of particles having a particle size of 45 μm or less is less than 10% by mass, it becomes difficult to fill the microcracks (width of several millimeters) with the spray material during the leveling operation.
On the other hand, when the content of particles having a particle size of more than 0.5 mm and less than 4 mm exceeds 50% by mass, the viscosity is lowered and the coke oven is easily peeled off from the coke oven carbonization chamber during the leveling operation. On the other hand, when the content of particles having a particle size of more than 0.5 mm and less than 4 mm is less than 20% by mass, the viscosity increases and the work load during the leveling operation increases.
In addition, this particle size structure is preferable also from the point which is easy to make the compressibility of a spraying material into 15% or more and 32% or less.
Here, in the present invention, the particle diameter of the particles exceeding d means that the particles remain on the sieve having an opening d, and the particle diameter of not more than d means that the particles are eyes. It means a particle size that passes through a sieve having an opening d.

本発明の吹付け施工方法で使用する吹付け材料は、耐火性粉末に加えて、結合剤、分散剤、急結剤といった添加剤を適宜含有し混合したものとすることができる、また、添加剤と共に繊維を含有することもできる。   The spraying material used in the spraying construction method of the present invention can be appropriately mixed and mixed with additives such as a binder, a dispersing agent and a quick setting agent in addition to the refractory powder. A fiber can also be contained with an agent.

耐火性粉末としては、一般的にコークス炉炭化室用不定形耐火物に使用される耐火性粉末であれば問題なく使用することができ、具体的には、シリカ質、アルミナ−シリカ質が挙げられる。   The refractory powder can be used without any problem as long as it is a refractory powder generally used for an amorphous refractory for a coke oven carbonization chamber, and specifically includes siliceous and alumina-silica. It is done.

結合剤としては、消石灰、アルミナセメント、マグネシアセメント、リン酸塩、ケイ酸塩などが挙げられ、これらのうち1種又は2種以上を組み合わせて使用することができる。   Examples of the binder include slaked lime, alumina cement, magnesia cement, phosphate, silicate, and the like, and one or more of these can be used in combination.

分散剤は解こう剤とも称され、吹付け材料の流動性を付与する効果をもつ。この分散剤としては、一般的な不定形耐火物で使用されているものであれば問題なく使用することができる。具体例としては、トリポリリン酸ソーダ、ヘキサメタリン酸ソーダ、ウルトラポリリン酸ソーダ、酸性ヘキサメタリン酸ソーダ、ホウ酸ソーダ、炭酸ソーダ、ポリメタリン酸塩、ケイ酸塩、リン酸塩などの無機塩、クエン酸ソーダ、酒石酸ソーダ、ポリアクリル酸ソーダ、スルホン酸ソーダ、ポリカルボン酸塩、β−ナフタレンスルホン酸塩類、ナフタリンスルフォン酸、カルボキシル基含有ポリエーテル系分散剤等である。   The dispersant is also called a peptizer and has the effect of imparting the fluidity of the spray material. As this dispersant, any dispersant used in general amorphous refractories can be used without any problem. Specific examples include sodium tripolyphosphate, sodium hexametaphosphate, sodium ultrapolyphosphate, sodium acid hexametaphosphate, sodium borate, sodium carbonate, polymetaphosphate, silicate, phosphate and other inorganic salts, sodium citrate, Examples thereof include sodium tartrate, sodium polyacrylate, sodium sulfonate, polycarboxylate, β-naphthalenesulfonate, naphthalene sulfonic acid, carboxyl group-containing polyether dispersant, and the like.

急結剤は施工水の存在下で結合剤と反応し、吹付け材料を急速に硬化させ、吹付け材料に付着性を付与する。急結剤は粉末状態で吹付け材料に当初から混入させておくほか、急結剤を先端吹付けノズル4又は注水器7より添加してもよい。急結剤を先端吹付けノズル4又は注水器7より添加する場合は、必要により急結剤を水で希釈した液状で使用する。
急結剤の具体例を挙げると、ケイ酸ナトリウム、ケイ酸カリウムなどのケイ酸塩、アルミン酸ナトリウム、アルミン酸カリウム、アルミン酸カルシウムなどのアルミン酸塩、炭酸ナトリウム、炭酸カリウム、炭酸水素ナトリウムなどの炭酸塩、硫酸ナトリウム、硫酸カリウム、硫酸マグネシウムなどの硫酸塩、CaO・Al、12CaO・7Al、CaO・2Al、3CaO・Al、3CaO・3Al・CaF、11CaO・7Al・CaFなどのカルシウムアルミネート類、酸化カルシウム、水酸化カルシウム、塩化カルシウムなどのカルシウム塩などである。
The rapid setting agent reacts with the binder in the presence of construction water to rapidly cure the spray material and impart adhesion to the spray material. The quick setting agent may be mixed in the spray material from the beginning in a powder state, or the quick setting agent may be added from the tip spray nozzle 4 or the water injector 7. When the quick setting agent is added from the tip spray nozzle 4 or the water injector 7, the quick setting agent is used in a liquid form diluted with water as necessary.
Specific examples of the quick setting agent include silicates such as sodium silicate and potassium silicate, aluminates such as sodium aluminate, potassium aluminate and calcium aluminate, sodium carbonate, potassium carbonate and sodium hydrogen carbonate. carbonates, sodium sulfate, potassium sulfate, sulfates such as magnesium sulfate, CaO · Al 2 O 3, 12CaO · 7Al 2 O 3, CaO · 2Al 2 O 3, 3CaO · Al 2 O 3, 3CaO · 3Al 2 O Calcium aluminates such as 3 · CaF 2 , 11CaO · 7Al 2 O 3 · CaF 2 , calcium salts such as calcium oxide, calcium hydroxide, and calcium chloride.

繊維は、通常の不定形耐火物で爆裂防止等の目的で使用されている繊維を使用することができ、例えば、ビニロン、ナイロン、PVA、ポリビニル、ポリスチレン、ポリプロピレン、炭素等である。   As the fiber, a fiber that is an ordinary amorphous refractory and used for the purpose of preventing explosion or the like can be used, and examples thereof include vinylon, nylon, PVA, polyvinyl, polystyrene, polypropylene, and carbon.

表1に、本発明の実施例及び比較例を示している。
吹付け材料は、耐火性粉末としてアルミナ−シリカ質粉末、結合剤として消石灰、及び分散剤としてケイ酸塩を所定の割合で混合したものとし、この吹付け材料を図1の吹付け装置にて、コークス炉炭化室の損傷箇所を模したシャモットれんがに対し吹付け、均し作業を行った。吹付け施工時、吹付け対象であるシャモットれんがは500℃に予熱した。
評価としては、吹付け施工時に混水性と搬送性を評価するとともに、均し作業の作業性と吹付け材料の充填性を評価し、これらの評価結果に基づいて総合評価を行った。
なお、搬送用ガス及び吹付け材料搬送用ガスの圧力は0.2MPa以上0.5MPa以下の範囲とした。
Table 1 shows examples and comparative examples of the present invention.
The spray material is a mixture of alumina-siliceous powder as a refractory powder, slaked lime as a binder, and silicate as a dispersant in a predetermined ratio. The chamoten brick was imitated to the damaged part of the coke oven carbonization chamber. At the time of spraying construction, the chamotte bricks to be sprayed were preheated to 500 ° C.
As evaluation, while evaluating water-mixing and conveyance at the time of spray construction, the workability of leveling work and the filling property of spray material were evaluated, and comprehensive evaluation was performed based on these evaluation results.
Note that the pressures of the transfer gas and the spray material transfer gas were in the range of 0.2 MPa to 0.5 MPa.

混水性は、先端吹付けノズル4からの吹付けの状態を目視で観察し、施工水と吹付け材料の分離の程度により評価した。この分離の程度が小さいほど混水性に優れるということである。具体的には、分離がない場合を○(優)、分離が小さい場合を△(良)、分離が大きい場合を×(不良)とした。   The mixed water was evaluated by visually observing the state of spraying from the tip spray nozzle 4 and by the degree of separation between the construction water and the spray material. The smaller the degree of separation, the better the water mixing. Specifically, the case where there was no separation was evaluated as ◯ (excellent), the case where separation was small was evaluated as Δ (good), and the case where separation was large was evaluated as x (defective).

搬送性は、先端吹付けノズル4からの吹付けの状態を目視で観察し、吹付け材料の吐出量の変動の程度により評価した。この吐出量の変動の程度が小さいほど搬送性に優れるということである。具体的には、吐出量の変動がない場合を○(優)、吐出量の変動が若干ある場合を△(良)、吐出量の変動が大きい場合を×(不良)とした。   The transportability was evaluated by visually observing the state of spraying from the tip spray nozzle 4 and by the degree of variation in the discharge amount of the spray material. The smaller the variation in the discharge amount, the better the transportability. Specifically, the case where there was no change in the discharge amount was indicated as ◯ (excellent), the case where there was a slight change in the discharge amount, Δ (good), and the case where the change in the discharge amount was large was indicated as x (defect).

均し作業の作業性は、均し作業時の均しやすさによって評価した。具体的には、均し作業時に抵抗が少なく容易に均すことができる場合を○(優)、抵抗が若干大きいが均すことはできる場合を△(良)、抵抗が大きく均すことが困難な場合を×(不良)とした。   The workability of the leveling work was evaluated by the leveling ease during the leveling work. Specifically, ○ (excellent) when resistance can be easily leveled with little resistance during leveling work, △ (good) when resistance is slightly large but can be leveled, and resistance is greatly leveled. The case where it was difficult was set as x (defect).

吹付け材料の充填性は、均し作業後に、吹付け対象であるシャモットれんがを図2に示すように切断し、この切断面における損傷箇所への吹付け材料の充填面積率によって評価した。具体的には、充填面積率が80%以上の場合を○(優)、充填面積率が60%以上80%未満の場合を△(良)、充填面積率が60%未満の場合を×(不良)とした。   The filling property of the spray material was evaluated by cutting the chamotte bricks to be sprayed as shown in FIG. 2 after the leveling work and by filling the damaged area on the cut surface with the spray material. Specifically, the case where the filling area ratio is 80% or more is ◯ (excellent), the case where the filling area ratio is 60% or more and less than 80% is Δ (good), and the case where the filling area ratio is less than 60% is × ( Bad).

総合評価は、前記の各評価において、全てが○(優)の場合を○(優)、いずれかに△(良)があり、かつ×(不良)がない場合を△(良)、いずれかに×(不良)がある場合を×(不良)とした。   Comprehensive evaluation, in each of the above evaluations, if all are ○ (excellent), ○ (excellent), if there is a △ (good), and if there is no × (bad), either △ (good) The case where there was a x (defect) was defined as x (defect).

Figure 0006393438
表1の実施例1〜14はいずれも、搬送用ガス流量比が0.07以上2以下、かつ吹付け材料の圧縮度が15%以上32%以下と本発明の範囲内にあり、各評価において×(不良)の評価はなく良好であり、総合評価も良好であった。
Figure 0006393438
Each of Examples 1 to 14 in Table 1 is within the scope of the present invention, with the transfer gas flow rate ratio being 0.07 or more and 2 or less, and the compressibility of the spray material being 15% or more and 32% or less. In the evaluation, x (defect) was not good, and the overall evaluation was good.

一方、比較例1は、吹付け材料の圧縮度が10%と小さい例である。均し作業の作業性が悪く、充填性も悪かった。   On the other hand, Comparative Example 1 is an example in which the compressibility of the spray material is as small as 10%. The workability of the leveling work was poor and the filling property was also bad.

1 材料供給機
2 吹付け材料
3 テーブルフィーダー
4 先端吹付けノズル
5 材料搬送管
6 吹付け材料搬送用ガス導入管
7 注水器
A コークス炉炭化室
DESCRIPTION OF SYMBOLS 1 Material supply machine 2 Spraying material 3 Table feeder 4 Tip spray nozzle 5 Material conveyance pipe 6 Gas introduction pipe for spraying material conveyance 7 Water injection device A Coke oven carbonization chamber

Claims (6)

材料供給機から先端吹付けノズルに至る材料搬送管に注水器を1つのみ設け、この注水器から材料搬送管内を搬送される吹付け材料に注水するコークス炉炭化室用不定形耐火物の吹付け施工方法であって、
前記注水器に導入される施工水を搬送するための施工水搬送用ガスの流量(Nm/min)と、吹付け材料を搬送するための吹付け材料搬送用ガスの流量(Nm/min)との比(施工水搬送用ガスの流量/吹付け材料搬送用ガスの流量)が0.07以上2以下であり、かつ、前記吹付け材料の圧縮度が15%以上32%以下である、コークス炉炭化室用不定形耐火物の吹付け施工方法。
Only one water injector is installed in the material transport pipe from the material feeder to the tip spray nozzle, and the spraying of the amorphous refractory for the coke oven carbonization chamber that injects water into the spray material transported through the material transport pipe from this water injector. It is an installation method,
The flow rate of the construction water carrier gas for transporting the construction water introduced into the water injector and (Nm 3 / min), the spraying material conveying gas for conveying the spraying material flow (Nm 3 / min ) (Flow rate of construction water carrying gas / flow rate of blowing material carrying gas) is 0.07 or more and 2 or less, and the compressibility of the blowing material is 15% or more and 32% or less. , A method for spraying amorphous refractories for coke oven carbonization chambers.
前記施工水搬送用ガスの流量(Nm/min)と施工水量(m/min)との比(施工水搬送用ガスの流量/施工水量)が100以上1000以下である、請求項1に記載のコークス炉炭化室用不定形耐火物の吹付け施工方法。 The ratio of the flow rate (Nm 3 / min) of the construction water carrying gas to the construction water amount (m 3 / min) (flow rate of construction water carrying gas / construction water amount) is 100 or more and 1000 or less. A method for spraying an amorphous refractory for a coke oven carbonization chamber as described. 吹付け材料の吐出量(kg/min)と搬送用ガスの合計流量(Nm/min)との比(吹付け材料の吐出量/搬送用ガスの合計流量)が1以上20以下である、請求項1又は2に記載のコークス炉炭化室用不定形耐火物の吹付け施工方法。 The ratio (discharge amount of spray material / total flow of transport gas) of the discharge amount of spray material (kg / min) and the total flow rate of transport gas (Nm 3 / min) is 1 or more and 20 or less. A method for spraying an amorphous refractory for a coke oven carbonization chamber according to claim 1 or 2. 吹付け材料中における粒径0.5mm超4mm以下の粒子の含有量が20質量%以上50質量%以下であり、粒径45μm以下の粒子の含有量が10質量%以上40質量%以下である、請求項1から3のいずれかに記載のコークス炉炭化室用不定形耐火物の吹付け施工方法。   The content of particles having a particle size of more than 0.5 mm and 4 mm or less in the spray material is 20% by mass or more and 50% by mass or less, and the content of particles having a particle size of 45 μm or less is 10% by mass or more and 40% by mass or less. A method for spraying an irregular refractory for a coke oven carbonization chamber according to any one of claims 1 to 3. 請求項1から4のいずれかに記載のコークス炉炭化室用不定形耐火物の吹付け施工方法に使用する吹付け材料であって、圧縮度が15%以上32%以下である、吹付け材料。   It is a spraying material used for the spray construction method of the amorphous refractory for coke oven carbonization chambers in any one of Claim 1 to 4, Comprising: The spraying material whose compression degree is 15% or more and 32% or less . 粒径0.5mm超4mm以下の粒子の含有量が20質量%以上50質量%以下であり、粒径45μm以下の粒子の含有量が10質量%以上40質量%以下である、請求項5に記載の吹付け材料。   The content of particles having a particle size of more than 0.5 mm and 4 mm or less is 20% by mass or more and 50% by mass or less, and the content of particles having a particle size of 45 μm or less is 10% by mass or more and 40% by mass or less. The spraying material described.
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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63289091A (en) * 1987-05-20 1988-11-25 Kawasaki Refract Co Ltd Nozzle for hot spraying repair of c gas passageway etc. of coke oven regenerator
JP2000192121A (en) * 1998-12-25 2000-07-11 Kawasaki Steel Corp Wet type spray-working method of prepared unshaped refractory
WO2005121676A1 (en) * 2004-06-07 2005-12-22 Krosakiharima Corporation Method of spray application of monolithic refractory, spray material for use therein, and application apparatus
JP2007008766A (en) * 2005-06-30 2007-01-18 Kurosaki Harima Corp Magnesian repairing material for dry type spraying operation
JP2011208837A (en) * 2010-03-29 2011-10-20 Plibrico Japan Co Ltd Device and method for spraying construction of unshaped refractory

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS63289091A (en) * 1987-05-20 1988-11-25 Kawasaki Refract Co Ltd Nozzle for hot spraying repair of c gas passageway etc. of coke oven regenerator
JP2000192121A (en) * 1998-12-25 2000-07-11 Kawasaki Steel Corp Wet type spray-working method of prepared unshaped refractory
WO2005121676A1 (en) * 2004-06-07 2005-12-22 Krosakiharima Corporation Method of spray application of monolithic refractory, spray material for use therein, and application apparatus
JP2007008766A (en) * 2005-06-30 2007-01-18 Kurosaki Harima Corp Magnesian repairing material for dry type spraying operation
JP2011208837A (en) * 2010-03-29 2011-10-20 Plibrico Japan Co Ltd Device and method for spraying construction of unshaped refractory

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