JP4370314B2 - Granulation method of highly dehydrated lime cake - Google Patents

Granulation method of highly dehydrated lime cake Download PDF

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JP4370314B2
JP4370314B2 JP2006209374A JP2006209374A JP4370314B2 JP 4370314 B2 JP4370314 B2 JP 4370314B2 JP 2006209374 A JP2006209374 A JP 2006209374A JP 2006209374 A JP2006209374 A JP 2006209374A JP 4370314 B2 JP4370314 B2 JP 4370314B2
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泰彦 河村
志摩夫 田中
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北海道糖業株式会社
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この発明は、製糖工場で大量に発生する高脱水ライムケーキの造粒方法の改良に関するものである。   The present invention relates to an improvement in a granulation method for a highly dehydrated lime cake that is generated in large quantities in a sugar factory.

従来製糖工場における砂糖製造工程において、ビートから抽出した糖液から不純物を取り除くために、糖液中に石灰乳を加え、これに炭酸ガスを吹き込む所謂炭酸飽充を行うことにより炭酸カルシウムの凝集物を生成し、これに不純物を吸着させる方法が採用されているが、これを濾過した残渣がライムケーキである。   In a sugar manufacturing process in a conventional sugar factory, in order to remove impurities from the sugar solution extracted from beet, lime milk is added to the sugar solution and carbon dioxide is blown into it, so-called carbonic acid saturation, and so on. Is used, and impurities are adsorbed on the lime cake. The residue obtained by filtering this is a lime cake.

一方、近年ライムケーキの減量化のために最終手段として専用のフィルタ−プレスを用いて濾過し、含水率27%〜33%まで脱水しているが、これを既存の含水率50%のものと区別するため高脱水ライムケーキと呼ばれている。   On the other hand, in order to reduce the amount of lime cake in recent years, it is filtered using a special filter press as a last resort and dehydrated to a moisture content of 27% to 33%. To distinguish, it is called highly dehydrated lime cake.

この高脱水ライムケーキの一部は主に農地の酸度矯正とカルシウムの補給を目的とし、専用散布機を利用して農地への散布等が行われている。   Part of this highly dehydrated lime cake is mainly used to correct the acidity of the farmland and replenish calcium, and is sprayed onto the farmland using a dedicated sprayer.

しかし 、高脱水ライムケーキは見た目には固形粉状であるが、約30%の水分を含んでいるので、このまま、散布機を使って散布を行うと、散布機の攪拌機構への付着、或いはホッパー内での付着のように落下阻害を起こすといった症状を呈するため、これらの散布機では高脱水ライムケーキが思うように使えないという欠点がある。   However, although the highly dehydrated lime cake looks like a solid powder, it contains about 30% of moisture, so if it is sprayed with a spreader as it is, it will adhere to the stirring mechanism of the spreader, or These sprayers have the disadvantage of not being able to use a highly dehydrated lime cake as expected because it presents symptoms such as falling in the hopper.

これらの現象を回避するために、高脱水ライムケーキ自体を造粒後強制乾燥する方法が試みられているが(特開平11-90203号、特開2002-331300)、粒状化して乾燥するコストは実用化する上で大きな障害となっている。   In order to avoid these phenomena, methods of forced drying after granulation of highly dehydrated lime cake itself have been tried (JP-A-11-90203, JP-A-2002-331300). This is a major obstacle to commercialization.

このため、本願発明者らは、大量に発生する高脱水ライムケーキを強制乾燥を伴わず、低コストで造粒化する方法として、先に高脱水ライムケーキに、適量の水とセメント類又はマグネシウム系固化剤の1種又は2種以上を加えて造粒方法を提案した(特願2005-368178)。
For this reason, the inventors of the present invention, as a method of granulating a highly dehydrated lime cake generated in large quantities without forced drying, at a low cost, to a highly dehydrated lime cake first, an appropriate amount of water and cement or magnesium. A granulation method was proposed by adding one or more of solidifying agents ( Japanese Patent Application No. 2005-368178 ).

しかし、この方法では得られた造粒品は一般には数mの高さに積み上げて十数日から数十日の間、養生・自然乾燥されるが、このため積み上げられた未養生の造粒品には外力が加わり、造粒品が不定形の粒子である場合、その一部が粉砕して、粉状になり、歩留まりが低下したり、或いはその自重により自然乾燥中或いは保管中に粒子同士の固結が発生する等の欠点がある。   However, the granulated product obtained by this method is generally piled up to a height of several meters and then cured and naturally dried for a few dozen days to several tens of days. When an external force is applied to the product and the granulated product is irregularly shaped particles, a part of the granulated product is pulverized and powdered, the yield decreases, or the particles are naturally dried or stored during storage due to their own weight. There are drawbacks such as the occurrence of solidification.

そこで、この発明は、上記造粒方法の改良として高脱水ライムケーキに、適量の水とセメント類又はマグネシウム系固化剤の1種又は2種以上を加えて造粒する造粒工程と、該造粒工程で得られた造粒品に補助剤を加えて整粒する整粒工程からなる高脱水ライムケーキの造粒方法を提案するものである。   Therefore, the present invention provides a granulation step of adding a suitable amount of water and one or more of cements or a magnesium-based solidifying agent to a highly dehydrated lime cake as an improvement of the above granulation method, The present invention proposes a granulation method of a highly dehydrated lime cake comprising a granulation step of adding an auxiliary agent to the granulated product obtained in the granulation step.

即ち、この発明では造粒工程で得られた未養生の造粒品は整粒工程で補助剤を加えて整粒されるため、不定形粒子は丸くなり、したがってこれを積み上げて養生・自然乾燥させてもその一部が粉砕して、粉状になり、歩留まりが低下したり、或いはその自重により自然乾燥中或いは保管中に粒子同士の固結が発生することはない。   That is, in this invention, the uncured granulated product obtained in the granulation process is sized by adding an auxiliary agent in the sizing process, so that the irregular shaped particles are rounded, and therefore, they are piled up to be cured and naturally dried. Even if it is made to part, the part will grind | pulverize and it will become a powder form, a yield will not fall, or solidification of particle | grains will not generate | occur | produce during natural drying or storage by the dead weight.

なお、補助剤を使用することなく整粒を行うと、粒子は装置内で充満するため、粒子同士の成長が進み、整粒終了時点の粒子は多少大きくなると共に、粒子同士が付着した歪な不定形の粒子となる。   In addition, when sizing without using an auxiliary agent, the particles are filled in the apparatus, so that the growth of the particles proceeds, the particles at the end of sizing become somewhat larger, and the particles adhere to each other. It becomes irregularly shaped particles.

これに対して、この発明のように補助剤を加えることにより粒子の成長は殆ど見られず、短時間で不定形粒子の丸みを改善することができ、しかも整粒工程において粒子の成長が抑制されるため、整粒時間を長くして更に整粒効果を高めることができ、同時に固結防止効果を高めることができる。   On the other hand, almost no particle growth is observed by adding an auxiliary agent as in the present invention, the roundness of the irregular shaped particles can be improved in a short time, and the particle growth is suppressed in the sizing process. Therefore, the sizing effect can be further increased by increasing the sizing time, and at the same time the anti-caking effect can be enhanced.

補助剤としては、タルクがライムケーキ同様にPHが高く、滑石と呼ばれる通り滑りがよく、ライムケーキ粒子に対する付着性もよく、更に肥料のキャリヤに使われており、安全性も高い等の理由から最も好ましい材料である。   As auxiliaries, talc has a high pH like lime cake, slips well as talc, has good adhesion to lime cake particles, and is also used as a fertilizer carrier, for high safety. Most preferred material.

この他、乾燥した粉状物であれば補助剤として使用可能であり、例えばフライアッシュ、石灰粉、鉱物粉、絶乾状のライムケーキ或いはステアリン酸などの油脂等が使用可能である。   In addition, any dry powder can be used as an auxiliary agent. For example, fly ash, lime powder, mineral powder, absolutely dry lime cake, or fats and oils such as stearic acid can be used.

なお、補助剤は整粒工程において造粒品に対して1〜4重量%程度加えられる。   In addition, an adjuvant is added about 1-4 weight% with respect to a granulated product in a granulation process.

一方、造粒工程で使用するセメント類としてはポルトランドセメント、高炉セメント、フライアッシュセメント、スラグセメント、シリカセメント、早強セメント、白色セメント、アークウィーン系セメント、アルミナセメント等の各種のセメント類を挙げることができ、特に農地等に散布するために使用する場合にはクロム溶出の少ない高炉セメントB種等が好ましい。   On the other hand, the cements used in the granulation process include various cements such as Portland cement, blast furnace cement, fly ash cement, slag cement, silica cement, early strength cement, white cement, Arkwien cement, and alumina cement. In particular, when used for spraying on agricultural land or the like, blast furnace cement type B with little chromium elution is preferable.

なお、フライアッシュセメントを造粒剤として使用する場合には、得られた造粒品は融雪剤として使用することもできるが、フライアッシュを含まないセメントを使用する場合にもフライアッシュを混合して造粒すれば、融雪剤として使用することもできる。   When fly ash cement is used as a granulating agent, the resulting granulated product can be used as a snow melting agent, but fly ash is also mixed when cement containing no fly ash is used. Can be used as a snow melting agent.

また、マグネシウム系固化剤としては純粋な酸化マグネシウムの他に、工業用酸化マグネシウム或いはマグネシウムを主成分とする固化剤を使用することができる。   In addition to pure magnesium oxide, industrial magnesium oxide or a solidifying agent mainly composed of magnesium can be used as the magnesium-based solidifying agent.

これらセメント類、マグネシウム系固化剤の1種又は2種以上は、造粒工程において高脱水ライムケーキに対して2.5重量%〜5重量%を添加して造粒が行われ、圧潰強度0.1〜0.2Kgの造粒品を得ることができる。   One or more of these cements and magnesium-based solidifying agents are granulated by adding 2.5% to 5% by weight to the highly dehydrated lime cake in the granulation step, and the crushing strength is 0.1 to 0.2. A granulated product of Kg can be obtained.

造粒工程、整粒工程においては、攪拌造粒装置、転動造粒装置何れも使用することができる。   In the granulation step and the granulation step, both a stirring granulation device and a rolling granulation device can be used.

しかし、整粒工程において攪拌造粒装置を使用すると、補助剤の必要量が造粒品に対して2重量%以上と多くなる。これは攪拌造粒装置を使用すると、最終的には丸みは改善されるが整粒工程開始時においてやや歪んだ不定形となり、この窪みを埋めるために補助剤を必要とすると考えられる。   However, if an agitation granulator is used in the granulation step, the required amount of the auxiliary agent increases to 2% by weight or more with respect to the granulated product. When a stirring granulator is used, the roundness is eventually improved, but it becomes an irregular shape that is slightly distorted at the start of the sizing process, and it is considered that an auxiliary agent is required to fill this recess.

これに対して、転動造粒装置では攪拌造粒装置に比べて粒子は丸みがあり、このため補助剤の必要量は造粒品に対して1〜2重量%で効果を得ることができ、したがって補助剤の使用量からすると攪拌造粒装置に比較して転動造粒装置が有利である。   On the other hand, in the rolling granulator, the particles are round compared to the stirring granulator, so that the required amount of the auxiliary agent can be effective at 1 to 2% by weight based on the granulated product. Therefore, the rolling granulator is more advantageous than the stirring granulator in view of the amount of the auxiliary agent used.

しかしながら、転動造粒装置では造粒初期での安定性にやや難があり、ダマが出来やすく造粒初期の粒子の核を揃えにくいといった難点から造粒時間が長くかかったり、大きな粒子が含まれ、歩留まりが低下するという欠点がある。   However, with the rolling granulator, the stability at the initial stage of granulation is somewhat difficult, and it takes a long time to granulate due to the difficulty that it is easy to be lumped and it is difficult to align the cores of the particles at the initial stage of granulation. Therefore, there is a disadvantage that the yield decreases.

これに対して攪拌造粒装置では造粒初期の均一な顆粒状の核となる粒子を安定して製造しやすく、したがって粒子が顆粒状となった段階で転動造粒装置に移し替えて整粒を行えば、造粒工程、整粒工程を効率的に行わせることができる。   In contrast, the agitation granulator facilitates stable production of uniform granular nuclei at the initial stage of granulation. Therefore, when the particles are granulated, they are transferred to a tumbling granulator. If granulation is performed, the granulation step and the sizing step can be performed efficiently.

以上要するに、この発明では造粒工程において高脱水ライムケーキにセメント類、マグネシウム系固化剤の1種又は2種以上を加えて得られた造粒品は整粒工程で補助剤を加えて整粒されるため、不定形粒子は丸くなり、したがってこれを積み上げて養生・自然乾燥させてもその一部が粉砕して、粉状になり、歩留まりが低下したり、或いはその自重により自然乾燥中或いは保管中に粒子同士の固結が発生することはない。   In short, in this invention, the granulated product obtained by adding one or more of cements and magnesium-based solidifying agents to the highly dehydrated lime cake in the granulation step is sized by adding an auxiliary agent in the granulation step. Therefore, even if the irregular shaped particles are rounded, and they are stacked and cured and naturally dried, some of them are crushed and become powdery, the yield decreases, or due to their own weight, During storage, the particles are not consolidated.

高脱水ライムケーキに、適量の水とセメント類又はマグネシウム系固化剤の1種又は2種以上を加えて造粒する造粒工程と、該造粒工程で得られた造粒品にタルク等の補助剤を加えて整粒する整粒工程からなる高脱水ライムケーキの造粒方法。   A granulation step of adding a suitable amount of water and one or more of cements or a magnesium-based solidifying agent to a highly dehydrated lime cake, and granulating the granulated product obtained in the granulation step, such as talc A granulation method for a highly dehydrated lime cake comprising a sizing step of adding an auxiliary agent and sizing.

実施例1
攪拌造粒装置(北川鉄工所製、ペレガイヤVZ−100E)又は転動造粒装置(北川鉄工所製、スプロアFZ−200)をそれぞれ単独で使用したこの発明の実施例を図1のフローチャートに基づいて説明する。
Example 1
Based on the flowchart of FIG. 1, the Example of this invention which used the stirring granulator (Kitakawa Iron Works, Peregiya VZ-100E) or the rolling granulator (Kitakawa Iron Works, Sproa FZ-200) each independently was used. I will explain.

まず、上記攪拌造粒装置又は転動造粒装置に50Kgの高脱水ライムケーキを投入し、大きなかたまりが無くなる解砕を行い、次に高炉セメントB種又は酸化マグネシウム等の添加剤を適量投入後、混練を行いよく混ぜ合わせ、次に凝集用の加水を行ってから造粒工程を開始する。造粒粒子が目的とする大きさに成長するまで行う。   First, 50 kg of highly dehydrated lime cake is put into the agitation granulator or tumbling granulator, pulverized so that there is no large lump, and then an appropriate amount of additives such as blast furnace cement type B or magnesium oxide is added. The granulation process is started after kneading and mixing well, and then adding water for aggregation. This is performed until the granulated particles grow to the desired size.

次に、補助剤としてタルクの1〜4重量%を造粒装置に添加して整粒工程を開始する。投入後タルクは1分以内にほぼ全体に行き渡り、そのまま数分間整粒工程を続けても粒子の成長はほとんど見られず、短時間で粒子の丸さは改善された。   Next, 1 to 4% by weight of talc is added to the granulator as an auxiliary agent to start the granulating step. After the addition, talc was distributed almost within 1 minute, and even if the sizing process was continued for several minutes, almost no particle growth was observed, and the roundness of the particles was improved in a short time.

得られた造粒品は積み上げて養生・自然乾燥し、更に篩い処理して製品とするが、整粒工程で丸さが改善されているため、積み上げて養生・自然乾燥させる際或いは積み上げて保管される際にも外力に対して壊れにくくなったばかりでなく、生産時点から保管中に至るまで固結は見られなかった。   The resulting granulated product is stacked, cured and naturally dried, and further sieved to obtain a product. Since the roundness is improved in the granulation process, it is stored when stacked and cured or naturally dried or stacked and stored. In addition to being hard to break against external forces, it was not consolidated from production to storage.

実施例2
攪拌造粒装置(北川鉄工所製、ペレガイヤVZ−100E)又は転動造粒装置(北川鉄工所製、スプロアFZ−200)を組み合わせて使用したこの発明の実施例を図2、図3のフローチャートに基づいて説明する。
Example 2
FIG. 2 and FIG. 3 are flowcharts of the embodiment of the present invention in which an agitation granulator (Kitakawa Iron Works, Pelegaia VZ-100E) or a rolling granulator (Kitakawa Steel Works, Sproa FZ-200) is used in combination. Based on

まず、上記攪拌造粒装置に50Kgの高脱水ライムケーキを投入後、解砕を行い、高炉セメントB種又は酸化マグネシウム等の添加剤を適量投入後、混練を行い、次に加水を行ってから造粒工程を開始するが、1mm以下の顆粒状の粒子まで成長させて造粒を終了する。   First, after adding 50 kg of highly dehydrated lime cake to the agitation granulator, pulverization is performed, an appropriate amount of additives such as blast furnace cement type B or magnesium oxide is added, kneading is performed, and then water is added. The granulation process is started, but the granulation is completed by growing to granulated particles of 1 mm or less.

次に顆粒状の造粒品を転動造粒装置に移し替えて目的とする大きさにまで成長させ、ここで補助剤としてタルクを1〜2重量%投入して整粒を1〜2分間行い、得られた造粒品は積み上げて養生・自然乾燥し、更に篩分け処理して製品とする。   Next, the granular granulated product is transferred to a tumbling granulator and grown to the desired size. Here, 1 to 2% by weight of talc is added as an auxiliary agent, and the sizing is performed for 1 to 2 minutes. The granulated product obtained is stacked, cured and air-dried, and further sieved to obtain a product.

なお、この実施例において造粒工程は5分以内で終了し、顆粒状の造粒品を転動造粒装置に移し替えてからの工程も5分以内で終了し、造粒、整粒にかかる時間は約10分以内である。   In this example, the granulation process is completed within 5 minutes, and the process after the granulated product is transferred to the tumbling granulator is also completed within 5 minutes. Such time is within about 10 minutes.

この実施例の方法では攪拌造粒装置では造粒を顆粒状までしか行われず、粒子が顆粒状となった段階で転動造粒装置に移し替えて整粒を行わせるものであり、しかも攪拌造粒装置から転動造粒装置にライムケーキ造粒品を移し終えると、攪拌造粒装置では次のバッチが開始できるため、造粒機1台ですべてを行うより全工程を効率的に短時間で終わらせることができる。   In the method of this example, the agitation granulator can only perform granulation to a granular form, and when the particles become granular, the particles are transferred to a tumbling granulator for sizing and stirring. When the lime cake granulated product has been transferred from the granulator to the rolling granulator, the next batch can be started with the agitation granulator, so the entire process can be shortened more efficiently than with a single granulator. Can be done in time.

即ち、この実施例は撹拌造粒装置と転動造粒装置の短所を避け、互いの装置の長所を組み合わせることにより製造効率を向上させるものであり、特に1バッチ500kg〜1トンの大型造粒装置による高脱水ライムケーキ処理に適した方法である。   That is, this embodiment avoids the disadvantages of the agitation granulator and the rolling granulator, and improves the production efficiency by combining the advantages of each other, especially large batch granulation of 500 kg to 1 ton per batch. This is a method suitable for high-dehydration lime cake processing using an apparatus.

以上要するに、この発明によれば高脱水ライムケーキにセメント類、マグネシウム系固化剤の1種又は2種以上を加えて得られた造粒品を養生・自然乾燥中或いは保管中の粉砕或いは粒子同士の固結を防止できる。   In short, according to the present invention, a granulated product obtained by adding one or more kinds of cements and magnesium-based solidifying agents to a highly dehydrated lime cake is ground or naturally dried or stored in storage. Can be prevented.

この発明の一実施例を示すフローチャートFlowchart showing one embodiment of the present invention この発明の他の実施例を示すフローチャートFlowchart showing another embodiment of the present invention 同上の実施例における造粒品の製造工程を示すフローチャートThe flowchart which shows the manufacturing process of the granulated product in an Example same as the above.

Claims (2)

高脱水ライムケーキに、セメント類又はマグネシウム系固化剤の1種又は2種以上を加え、更に凝集用の加水を行って造粒する造粒工程と、該造粒工程で得られた造粒品に補助剤としてタルクを加えて整粒する整粒工程と、得られた造粒品を積み上げて養生・自然乾燥する工程からなる高脱水ライムケーキの造粒方法。 A granulation step in which one or more cements or magnesium-based solidifying agents are added to a highly dehydrated lime cake, followed by addition of water for aggregation, and a granulated product obtained in the granulation step A granulation method of a highly dehydrated lime cake comprising a sizing step of adding talc as an auxiliary agent to sizing and a step of stacking the obtained granulated product and curing and drying naturally . 造粒工程において攪拌造粒装置を使用し、整粒工程において転動造粒装置を使用する請求項1の方法。 The method according to claim 1, wherein a stirring granulator is used in the granulation step, and a rolling granulator is used in the granulation step .
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