JPH0240954B2 - KAITENSHOSEIRONOSASUPENSHONPUREHIITAANIOKERUGENRYOFUNMATSUFUCHAKUBOSHIHOHO - Google Patents
KAITENSHOSEIRONOSASUPENSHONPUREHIITAANIOKERUGENRYOFUNMATSUFUCHAKUBOSHIHOHOInfo
- Publication number
- JPH0240954B2 JPH0240954B2 JP26745486A JP26745486A JPH0240954B2 JP H0240954 B2 JPH0240954 B2 JP H0240954B2 JP 26745486 A JP26745486 A JP 26745486A JP 26745486 A JP26745486 A JP 26745486A JP H0240954 B2 JPH0240954 B2 JP H0240954B2
- Authority
- JP
- Japan
- Prior art keywords
- suspension preheater
- raw material
- coating
- material powder
- adhesion
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 239000002994 raw material Substances 0.000 claims description 28
- 239000000725 suspension Substances 0.000 claims description 24
- 239000000843 powder Substances 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 12
- 238000010304 firing Methods 0.000 claims description 10
- 239000000546 pharmaceutical excipient Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 239000000463 material Substances 0.000 claims description 6
- 239000000126 substance Substances 0.000 claims description 6
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 239000011230 binding agent Substances 0.000 claims description 4
- 239000002612 dispersion medium Substances 0.000 claims description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 3
- 239000011247 coating layer Substances 0.000 claims description 3
- 229910052582 BN Inorganic materials 0.000 claims description 2
- PZNSFCLAULLKQX-UHFFFAOYSA-N Boron nitride Chemical compound N#B PZNSFCLAULLKQX-UHFFFAOYSA-N 0.000 claims description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 2
- 239000004115 Sodium Silicate Substances 0.000 claims description 2
- 229920002472 Starch Polymers 0.000 claims description 2
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical compound O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 claims description 2
- 239000010439 graphite Substances 0.000 claims description 2
- 229910002804 graphite Inorganic materials 0.000 claims description 2
- 239000010445 mica Substances 0.000 claims description 2
- 229910052618 mica group Inorganic materials 0.000 claims description 2
- 239000002480 mineral oil Substances 0.000 claims description 2
- 235000010446 mineral oil Nutrition 0.000 claims description 2
- CWQXQMHSOZUFJS-UHFFFAOYSA-N molybdenum disulfide Chemical compound S=[Mo]=S CWQXQMHSOZUFJS-UHFFFAOYSA-N 0.000 claims description 2
- 229910052982 molybdenum disulfide Inorganic materials 0.000 claims description 2
- 239000003921 oil Substances 0.000 claims description 2
- 239000011347 resin Substances 0.000 claims description 2
- 229920005989 resin Polymers 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 2
- 229910052911 sodium silicate Inorganic materials 0.000 claims description 2
- 239000008107 starch Substances 0.000 claims description 2
- 235000019698 starch Nutrition 0.000 claims description 2
- ITRNXVSDJBHYNJ-UHFFFAOYSA-N tungsten disulfide Chemical compound S=[W]=S ITRNXVSDJBHYNJ-UHFFFAOYSA-N 0.000 claims description 2
- 239000011248 coating agent Substances 0.000 description 17
- 238000000576 coating method Methods 0.000 description 15
- 239000004568 cement Substances 0.000 description 7
- 239000007789 gas Substances 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 239000010410 layer Substances 0.000 description 3
- 235000019738 Limestone Nutrition 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 239000006028 limestone Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 239000011398 Portland cement Substances 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 239000011449 brick Substances 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000011812 mixed powder Substances 0.000 description 1
- 235000011837 pasties Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 238000002018 water-jet injection Methods 0.000 description 1
Landscapes
- Muffle Furnaces And Rotary Kilns (AREA)
- Furnace Details (AREA)
Description
〔産業上の利用分野〕
この発明は例えばセメントや耐火原料などのク
リンカーを焼成する回転炉に付設されたサスペン
シヨンプレヒーターの内壁に通過原料が付着し次
いで固着しコーテイング状態となることを防止す
る方法に関するものである。
〔従来の技術〕
回転焼成炉(ロータリーキルン)の大型化とと
もに熱効率の向上と据え付け面積の有利性のため
サスペンシヨンプレヒーターが付設されているも
のが多く、これによつてロータリーキルンに送り
込む直前の原料粉末を上方から数段のサイクロン
中に順次導き、下方から約1000℃のキルン排ガス
を導入して予熱するものである。
第1図はセメントクリンカー焼成用のロータリ
ーキルンとサスペンシヨンプレヒーターの全体装
置の概略を示す斜視図である。図において1は高
さ約70mのサスペンシヨンプレヒーターで石灰石
と粘土を主体とする粉体の調合原料が上部の原料
装入口2から投入され、サイクロン3a,3b,
3c,3dおよび各サイクロンを連結するダクト
4a,4b,4c,4dを通過する間に充分に予
熱されて投入口チヤンバー5に落下し、この投入
口チヤンバー5からロータリーキルン6に原料が
供給されるようになつている。
ロータリーキルン6は周知のように傾斜したキ
ルンの回転によつて原料をキルンバーナー7の方
向に順次移動させ、バーナー近くの焼成帯部で最
終的に1500℃前後で焼成されてクリンカーとな
る。
この際燃焼ガスがサスペンシヨンプレヒーター
側に吸引されサスペンシヨンプレヒーター下部の
投入口チヤンバー5を通過する。この時排ガスの
温度は1000℃〜1200℃であり、サスペンシヨンプ
レヒーターにおける原料の主たる予熱熱源であ
る。なお第1図において8は高温のクリンカーを
冷却するクーラー、9はクーラー抽気管であり、
この管を通じてクーラー8内の高温ガスをも又サ
スペンシヨンプレヒーターに吸引されている。
〔発明が解決しようとする問題点〕
サスペンシヨンプレヒーターは前述のような構
造であり、予熱効率を高めるため投入された原料
は各サイクロン内を回転しながら順次落下するよ
うになつており、また投入口チヤンバー5内にお
いても原料の動きの多い状態である。さらに粉末
石灰石と粘土の混合物は加熱によつて仮焼反応が
進行するためにキルンの稼働1〜2日後から上記
原料粉末が投入口チヤンバーの内壁に付着し始
め、やがて成長して前面コーテイングの状態、さ
らに高温加熱されて岩石の如き硬い固着物(以下
これを「コーテイング」と呼称する)の層が全内
壁面に形成されるのである。
このまま長時間操業を続行するとサスペンシヨ
ンプレヒーターの各内部が狭くなり、やがて各ダ
クト内、投入口チヤンバー内に原料が詰つて、キ
ルンへの原料供給に重大な支障をきたすことにな
る。又、圧力損失が増大し排ガス吸引用フアン
(I.D.FAN)の運転にも影響を及ぼす様になる。
このような原料粉末のコーテイングの状態は、
例えば投入口チヤンバーにおいて、キルン稼働約
48時間で厚さ250mm〜300mmに達する。従つてセメ
ントロータリーキルンにおいては稼働中に1日3
回、多い時には1日5〜6回このコーテイングの
除去作業を行つているのが現状である。
ところがロータリーキルンは24時間連続運転、
かつサスペンシヨンプレヒーター内も高温である
ため内部にはいることができないので、従来は必
要箇所に20cm角位の作業窓も設けここから高圧
(250〜300Kg/cm2圧)の水流を内壁面に噴射し、
加水反応によつて体積膨張したコーテイングを吹
き飛ばす方法でコーテイング除去を行つていた。
これに必要とする水量は1回毎に約300、1
日1〜1.5tonに達し、この水分はプレヒーター内
部で蒸発させる必要があるため莫大な熱カロリー
が消費されるだけでなく、除去作業中は外気の吸
引を合せてプレヒーターの予熱効率が大幅に低下
するために、セメントクリンカーの焼出し量も標
準時の90〜97%に減少せねならず、また水蒸気の
大量発生によつて他の部位における原料粉末の固
着をも助長するという多くの問題点があつた。
この発明はかかる問題点を解決するためになさ
れたもので、サスペンシヨンプレヒーター各部の
内壁に投入原料が付着し難くなる方法を提供する
ことを目的とする。
〔問題点を解決するための手段〕
この発明にかかるサスペンシヨンプレヒーター
の付着防止方法は、サスペンシヨンプレヒーター
において、投入原料が通過する各部の内壁特に従
来クリンカー固着の著しい箇所(固着の状態はロ
ータリーキルンによつて異る)に、層状格子構造
物質と耐熱結合材と展着物質および分散媒とから
なる賦形剤を層状に塗布するものである。
しかして層状格子構造物質としては黒鉛、二硫
化モリブデン、二硫化タングステン、窒化硼素、
マイカの一種又は二種以上を、耐熱結合材として
はアルミナ、シリカのうち一種または二種を、展
着物質としては澱粉、レジン、珪酸ソーダ、燐酸
アルミニウムを使い、展着物質の分散媒としても
水もしくは鉱物油または合成油をそれぞれ配合し
た賦形剤を塗布するものである。
〔作用〕
賦形剤に含有される層状格子構造物質はその層
状の結晶構造に由来して大きい滑性作用を有する
もので併せて耐熱性をも有する物質として最良で
ある。
耐熱結合材を含有させるのは、賦形剤が塗布さ
れたのち高温ガスにより受ける熱によつて一部が
ガラス化し被覆層を強固に接着固化させるためで
ある。有機又は無機の展着物質を含有させるのは
後記する分散媒により塗布剤をペースト状もしく
はスプレー可能な流体とし、これにレンガ及びキ
ヤスタブル表面への展着、固着性を付与すると共
に、塗布後の加熱によつて表層が炭化されるので
さらに原料粉末が付着し難くなるものである。
また塗布層は加熱の進行に伴つて熱膨張をし内
壁との間に間隙を形成し易いのでコーテイングが
固着した場合も一緒にはがれ易い特性を有してい
る。
〔実施例〕
この発明をNセメント会社M工場のロータリー
キルンに付設のサスペンシヨンプレヒーターに実
施した状況について説明する。
実施した設備:
ロータリーキルン
直径 4.2m、長さ61m
回転数 3回転/Min
ポートランドセメントクリンカー焼成用キルンサ
スペンシヨンプレヒーター
高さ 70M NSF式
粉体原料投入量 190ton/時
投入口キヤンバー付近排ガス温度 1030〜1100
℃
内壁の材質 塩基性耐火レンガ
[Industrial Application Field] This invention prevents passing raw materials from adhering to the inner wall of a suspension preheater attached to a rotary furnace for firing clinker such as cement or refractory raw materials, and then becoming stuck and forming a coating state. It is about the method. [Prior art] As rotary kilns become larger, many of them are equipped with a suspension preheater to improve thermal efficiency and take advantage of installation space. The kiln is sequentially guided from above into several stages of cyclones, and kiln exhaust gas at approximately 1000°C is introduced from below to preheat it. FIG. 1 is a perspective view schematically showing the entire apparatus of a rotary kiln and a suspension preheater for firing cement clinker. In the figure, 1 is a suspension preheater with a height of approximately 70 m, and mixed powder raw materials mainly consisting of limestone and clay are inputted from the raw material charging port 2 at the top, and the cyclones 3a, 3b,
3c, 3d and ducts 4a, 4b, 4c, 4d connecting each cyclone, the raw material is sufficiently preheated and falls into the input chamber 5, from which the raw material is supplied to the rotary kiln 6. It's getting old. As is well known, the rotary kiln 6 sequentially moves the raw material in the direction of the kiln burner 7 by rotation of the inclined kiln, and is finally fired at around 1500°C in the firing zone near the burner to become clinker. At this time, the combustion gas is sucked toward the suspension preheater and passes through the inlet chamber 5 at the bottom of the suspension preheater. At this time, the temperature of the exhaust gas is 1000°C to 1200°C, and is the main preheating heat source for the raw material in the suspension preheater. In Fig. 1, 8 is a cooler for cooling the high-temperature clinker, 9 is a cooler bleed pipe,
The high temperature gas in the cooler 8 is also drawn into the suspension preheater through this pipe. [Problems to be solved by the invention] The suspension preheater has the above-mentioned structure, and in order to increase the preheating efficiency, the input raw materials fall sequentially while rotating inside each cyclone. There is also a lot of movement of raw materials within the input chamber 5. Furthermore, as the mixture of powdered limestone and clay undergoes a calcination reaction when heated, the raw material powder starts to adhere to the inner wall of the input chamber after 1 to 2 days of operation of the kiln, and eventually grows to form a front coating. Then, by further heating to a high temperature, a layer of hard, rock-like solid matter (hereinafter referred to as "coating") is formed on the entire inner wall surface. If the operation continues for a long period of time, the interior of the suspension preheater will become narrow, and eventually the ducts and input chambers will become clogged with raw materials, which will seriously impede the supply of raw materials to the kiln. In addition, the pressure loss will increase, which will affect the operation of the exhaust gas suction fan (IDFAN). The coating state of such raw material powder is
For example, in the input chamber, approximately
It reaches a thickness of 250mm to 300mm in 48 hours. Therefore, in a cement rotary kiln, 3
Currently, this coating removal work is carried out 5 to 6 times a day, sometimes 5 to 6 times a day. However, rotary kilns operate continuously for 24 hours.
In addition, since the inside of the suspension preheater is also high temperature, it is impossible to enter inside, so conventionally, we have installed working windows of about 20 cm square in the necessary places, and from these windows, a high pressure (250 to 300 kg/cm 2 pressure) water flow is directed to the inner wall surface. inject into;
The coating was removed by blowing off the coating that had expanded in volume due to the hydration reaction. The amount of water required for this is approximately 300,1
The amount of water reaches 1 to 1.5 tons per day, and this water needs to be evaporated inside the preheater, which not only consumes a huge amount of heat calories, but also draws in outside air during the removal process, which significantly increases the preheating efficiency of the preheater. Due to this, the amount of cement clinker baked out has to be reduced to 90-97% of the standard amount, and the large amount of water vapor generated also promotes the sticking of raw material powder in other parts, which is a problem. The dot was hot. The present invention was made to solve this problem, and an object of the present invention is to provide a method that makes it difficult for input raw materials to adhere to the inner walls of various parts of the suspension preheater. [Means for Solving the Problems] The method for preventing adhesion of a suspension preheater according to the present invention is applied to the inner wall of each part through which input raw materials pass through in a suspension preheater, particularly in areas where conventional clinker is significantly adhered (the state of adhesion is (depending on the rotary kiln), an excipient consisting of a layered lattice structure material, a heat-resistant binder, a spreading material, and a dispersion medium is applied in layers. However, the layered lattice structure materials include graphite, molybdenum disulfide, tungsten disulfide, boron nitride,
One or more types of mica is used, one or two types of alumina and silica are used as the heat-resistant binder, starch, resin, sodium silicate, and aluminum phosphate are used as the spreading substance, and it also serves as a dispersion medium for the spreading substance. An excipient containing water, mineral oil, or synthetic oil is applied. [Function] The layered lattice structure substance contained in the excipient has a large lubricity effect due to its layered crystal structure, and is best as a substance that also has heat resistance. The reason why the heat-resistant binder is included is that after the excipient is applied, a portion of the excipient becomes vitrified by the heat received from the high-temperature gas, thereby firmly adhering and solidifying the coating layer. The purpose of containing an organic or inorganic spreading substance is to make the coating agent into a pasty or sprayable fluid using a dispersion medium, which will be described later, and to impart spreading and adhesion properties to the brick and castable surfaces, as well as to improve the coating properties after coating. Since the surface layer is carbonized by heating, it becomes even more difficult for the raw material powder to adhere to it. Furthermore, the coated layer thermally expands as heating progresses and tends to form a gap with the inner wall, so that even if the coating is stuck, it is likely to peel off. [Example] A situation in which the present invention was applied to a suspension preheater attached to a rotary kiln of N Cement Company M Plant will be described. Equipment used: Rotary kiln Diameter 4.2m, Length 61m Rotation speed 3 rotations/Min Kiln suspension preheater for Portland cement clinker firing Height 70M NSF type Powder raw material input rate 190ton/hour Exhaust gas temperature near input camber 1030~ 1100
℃ Inner wall material Basic firebrick
上記それぞれの塗布作業試験を3回宛繰返した
結果、第1回試験では操業15日後において原料粉
末の付着はそれぞれの賦形剤ともにほとんどな
く、20日後において厚さ約15mmの原料粉末の付着
があつたが従来とは異つて、非常に柔かい付着で
あるため軽い振動を与えることにより高圧水流を
使用せずに簡単に剥離した。キルン運転中に塗布
したものは、約21日後同様に厚さ約15cmの原料粉
末の付着があつたが前記同様の簡単な作業にて剥
離した。
以上、繰り返した結果、従来の毎日3回のクリ
ンカー除去作業は全く必要がなくなり、たまには
付着しても軽い振動を与えることにより簡単に剥
離するため、従来の高圧水流を使用する除去作業
は行われず所要水量は従来作業では月30t〜40tで
あつたものが0となつた。
ところで上記説明はこの発明をサスペンシヨン
プレヒーター投入口チヤンバーにおいて使用した
場合についで述べたが、サスペンシヨンプレヒー
ターの他の部位の原料粉末付着防止にも使用でき
ることは勿論であり、またセメントクリンカー焼
成設備に限らず、石灰、ドロマイト、マグネシア
クリンカー、アルミナ等の焼成用ロータリキルン
に付設するサスペンシヨンプレヒーターにも塗布
剤の配合を調整することによつてこの実施例と同
様の結果を期待できる。
〔発明の効果〕
この発明は以上説明したとおり、原料粉末が固
着し易いサスペンシヨンプレヒーターの内壁に、
特殊配合の賦形剤の塗布層を形成させるという簡
単な方法により、原料粉末の付着を著しく減少せ
しめることができるのでセメント焼成設備の操業
において次のような効果がある。
1) 従来のコーテイング除去作業による予熱効
率の低下―原料投入量の減少−焼成クリンカー
の減産がなくなり、製品の生産性を3〜5%向
上させることができる。
2) 従来のコーテイング除去作業に伴う水分の
大量蒸発と多数回の外気吸引がなくなり熱カロ
リーのロスを大幅に低減できる。
3) コーテイング除去作業が従来の約1/40で足
り、労働力、作業時間ともに大幅に低下せしめ
るとともに従来の危険な作業をなくした。
4) 高圧水流噴射に伴う内張り耐火物の損粍が
なくなり、炉材の使用命数が長くなつた。
5) 従来の高圧水使用量30t〜40t/月を全く使
用する必要がなくなつた。
As a result of repeating each of the above coating work tests three times, it was found that in the first test, there was almost no adhesion of raw material powder for each excipient after 15 days of operation, and after 20 days, there was no adhesion of raw material powder with a thickness of about 15 mm. Unlike conventional Atsuta, the adhesion was very soft, so it was easily peeled off by applying light vibrations without using high-pressure water jets. When the coating was applied during kiln operation, about 21 days later, raw material powder of about 15 cm in thickness remained attached, but it was peeled off by the same simple operation as above. As a result of repeating the above, the conventional clinker removal work three times a day is no longer necessary, and even if it occasionally sticks, it is easily peeled off by applying light vibrations, so the conventional removal work using high-pressure water jets is no longer performed. The amount of water required for conventional work was 30 to 40 tons per month, but it has been reduced to zero. By the way, the above explanation was given regarding the case where this invention is used in the suspension preheater inlet chamber, but it can of course also be used to prevent the adhesion of raw material powder to other parts of the suspension preheater, and it can also be used for cement clinker firing. The same results as in this example can be expected by adjusting the formulation of the coating agent not only in the equipment but also in a suspension preheater attached to a rotary kiln for firing lime, dolomite, magnesia clinker, alumina, etc. [Effects of the Invention] As explained above, the present invention provides a method to prevent raw material powder from adhering to the inner wall of the suspension preheater, where raw material powder tends to stick.
The simple method of forming a coating layer of specially formulated excipients can significantly reduce the adhesion of raw material powder, resulting in the following effects in the operation of cement firing equipment. 1) Decrease in preheating efficiency due to conventional coating removal work - reduction in raw material input - reduction in production of fired clinker is eliminated, and product productivity can be improved by 3 to 5%. 2) The large amount of water evaporation and the multiple suction of outside air associated with conventional coating removal work are eliminated, and the loss of thermal calories can be significantly reduced. 3) The coating removal work is approximately 1/40th of the conventional work, significantly reducing both the labor force and working time, and eliminating the dangerous work that was previously required. 4) Damage to the lining refractory caused by high-pressure water jet injection has been eliminated, extending the useful life of the furnace material. 5) It is no longer necessary to use the conventional high-pressure water usage of 30 to 40 tons/month.
第1図は回転焼成炉とこれに付設するサスペン
シヨンプレヒーターの装置概略を示す斜視図であ
る。
図において、1……サスペンシヨンプレヒータ
ー、6……回転焼成炉。
FIG. 1 is a perspective view schematically showing a rotary firing furnace and a suspension preheater attached thereto. In the figure, 1 ...suspension preheater, 6...rotary firing furnace.
Claims (1)
に黒鉛、二硫化モリブデン、二硫化タングステ
ン、窒化硼素、マイカ等の層状格子構造物質の一
種又は二種以上と、アルミナ、シリカ等の耐熱結
合材の一種又は二種と、澱粉、レジン、珪酸ソー
ダ、燐酸アルミニウム等の有機又は無機の展着物
質、及びその分散媒としての水、もしくは鉱物
油、又は合成油とよりなる賦形財の塗布層を形成
せしめることを特徴とする回転焼成炉のサスペン
シヨンプレヒーターにおける原料粉末付着防止方
法。1. One or more layered lattice structure materials such as graphite, molybdenum disulfide, tungsten disulfide, boron nitride, mica, etc. and one or two heat-resistant binders such as alumina, silica, etc. are added to the necessary locations on the inner wall of the suspension preheater. Forming a coating layer of an excipient consisting of seeds, an organic or inorganic spreading substance such as starch, resin, sodium silicate, or aluminum phosphate, and water, mineral oil, or synthetic oil as a dispersion medium. A method for preventing the adhesion of raw material powder in a suspension preheater of a rotary firing furnace, characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26745486A JPH0240954B2 (en) | 1986-11-12 | 1986-11-12 | KAITENSHOSEIRONOSASUPENSHONPUREHIITAANIOKERUGENRYOFUNMATSUFUCHAKUBOSHIHOHO |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26745486A JPH0240954B2 (en) | 1986-11-12 | 1986-11-12 | KAITENSHOSEIRONOSASUPENSHONPUREHIITAANIOKERUGENRYOFUNMATSUFUCHAKUBOSHIHOHO |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS63123984A JPS63123984A (en) | 1988-05-27 |
| JPH0240954B2 true JPH0240954B2 (en) | 1990-09-13 |
Family
ID=17445068
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26745486A Expired - Lifetime JPH0240954B2 (en) | 1986-11-12 | 1986-11-12 | KAITENSHOSEIRONOSASUPENSHONPUREHIITAANIOKERUGENRYOFUNMATSUFUCHAKUBOSHIHOHO |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0240954B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0261158U (en) * | 1988-10-28 | 1990-05-07 |
-
1986
- 1986-11-12 JP JP26745486A patent/JPH0240954B2/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0261158U (en) * | 1988-10-28 | 1990-05-07 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63123984A (en) | 1988-05-27 |
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