JPH02120288A - Method for granulating crude bone fertilizer substrate, such as shell fossil - Google Patents
Method for granulating crude bone fertilizer substrate, such as shell fossilInfo
- Publication number
- JPH02120288A JPH02120288A JP63272790A JP27279088A JPH02120288A JP H02120288 A JPH02120288 A JP H02120288A JP 63272790 A JP63272790 A JP 63272790A JP 27279088 A JP27279088 A JP 27279088A JP H02120288 A JPH02120288 A JP H02120288A
- Authority
- JP
- Japan
- Prior art keywords
- drying
- pan
- mixing
- pulverizing
- granulation
- 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.)
- Granted
Links
- 239000003337 fertilizer Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title claims abstract description 17
- 210000000988 bone and bone Anatomy 0.000 title claims abstract description 9
- 239000000758 substrate Substances 0.000 title abstract 4
- 239000000463 material Substances 0.000 claims abstract description 38
- 238000002156 mixing Methods 0.000 claims abstract description 20
- 238000001035 drying Methods 0.000 claims abstract description 14
- 239000011230 binding agent Substances 0.000 claims abstract description 5
- 235000015170 shellfish Nutrition 0.000 claims description 5
- 238000005469 granulation Methods 0.000 abstract description 25
- 230000003179 granulation Effects 0.000 abstract description 25
- 239000002994 raw material Substances 0.000 abstract description 15
- 238000010298 pulverizing process Methods 0.000 abstract description 9
- 101150006573 PAN1 gene Proteins 0.000 abstract description 8
- 239000008187 granular material Substances 0.000 abstract description 4
- 230000008439 repair process Effects 0.000 abstract description 4
- 238000012544 monitoring process Methods 0.000 abstract description 2
- 239000002801 charged material Substances 0.000 abstract 1
- 239000011369 resultant mixture Substances 0.000 abstract 1
- 230000008569 process Effects 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 230000000694 effects Effects 0.000 description 7
- 239000000843 powder Substances 0.000 description 5
- 239000007788 liquid Substances 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- 235000008429 bread Nutrition 0.000 description 3
- 239000006185 dispersion Substances 0.000 description 3
- 239000007921 spray Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 2
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- 238000010793 Steam injection (oil industry) Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 235000013339 cereals Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000012937 correction Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000009313 farming Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000000265 homogenisation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 235000015097 nutrients Nutrition 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Fertilizers (AREA)
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、粗骨肥料基材の粒状化方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for granulating a coarse bone fertilizer base material.
近年、農業事情を取り巻く環境は厳しく、肥料業界もそ
の影響により、農作業の省力化、生産費の節減を図る目
的から粒状肥料の要請が多くなっている。In recent years, the environment surrounding agriculture has been severe, and the fertilizer industry has been affected by this, with an increasing number of requests for granular fertilizers for the purpose of saving labor in farming and reducing production costs.
従来、粗骨肥料基材の粒状化については、主として粉砕
を容易にし製品の圧密炭を上げる目的から、第１図に示
すように、まず基材を粗砕して乾燥してから粉砕する。Conventionally, with regard to granulation of coarse bone fertilizer base material, the base material is first coarsely crushed, dried, and then crushed, as shown in FIG. 1, mainly for the purpose of facilitating crushing and producing compacted coal as a product.
そしてこれに肥料成分を補完する副資材と、造粒に必要
な結合材とを混入し、混練して造粒したものを分級し、
乾燥して製品化する方法が採用されていた。Then, auxiliary materials that complement the fertilizer components and binding materials necessary for granulation are mixed in, kneaded, and granulated, which is then classified.
The method used was to dry and commercialize the product.
なお、粗骨肥料基材としては、貝化石や貝の捨て殻、動
物の骨、肥料用岩石、育苗床上原料等が挙げられる。こ
のうち、貝化石は、主に北陸、北海道、入用および東北
に産出するもので、従来から乾燥粉末化して肥料として
使用されているが、土壌中で緩慢に溶解・反応し、土壌
酸性を長期に亘り矯正し、作物に窒素、リン酸、カリ等
の主要な養分吸収を促進させる等の優れた機能が認めら
れるために最近注目されているので、特に造粒化の要請
が強い。In addition, examples of the coarse bone fertilizer base material include fossil shells, discarded shells of shells, animal bones, rocks for fertilizers, raw materials on seedling beds, and the like. Among these, shellfish fossils are mainly produced in Hokuriku, Hokkaido, Iyu, and Tohoku. Traditionally, they have been dried and powdered and used as fertilizer, but they dissolve and react slowly in the soil, reducing soil acidity. Recently, it has been attracting attention due to its excellent functions such as long-term correction and promoting the absorption of major nutrients such as nitrogen, phosphoric acid, and potassium in crops, so there is a strong demand for its granulation.
従来の粗骨肥料基材の粒状化方法によれば、上述の如く
、基材をまず粉体にする工程を経てから造粒工程に移行
するために種々の問題があった。According to the conventional method of granulating a coarse bone fertilizer base material, as mentioned above, there are various problems because the base material is first pulverized through a process and then transferred to a granulation process.
すなわち、基材から粉体（粉末、微粉）を得るには、殊
に含有水分の高い基材であれば、乾燥及び粉砕工程が必
要であり、それには広い土地、熱エネルギー、労働力等
が必要とされ、時には公害の補償の問題も生じてくるこ
とから、製品がどうしてもコスト高となることは避けら
れなかった。That is, in order to obtain powder (powder, fine powder) from a base material, especially if the base material has a high moisture content, drying and pulverization processes are necessary, which requires a large amount of land, thermal energy, labor, etc. Because of the necessity and sometimes the problem of compensation for pollution, it was inevitable that the product would be expensive.
加えて、乾燥・粉砕調整された原料に副資材や粒状化促
進材を計量し混合する混練工程が必要であるが、これも
前記と同様に、設備設置に伴う土地、設備投資、エネル
ギー、騒音防止対策を要し、また、粒状化促進材が液体
の場合は、摩擦による水分の発熱があり、主としてこの
ことが原因で、排気誘導設備ならびに排気誘導系路の閉
塞現象の防止対策、補修費、労務費を必要とし、併せて
各設備間の連続化輸送機器が必要である。In addition, a kneading process is required to measure and mix auxiliary materials and granulation promoters into the dried and pulverized raw materials, but this also requires land, capital investment, energy, and noise associated with equipment installation. In addition, when the granulation accelerator is a liquid, water heats up due to friction, and this is the main cause, requiring preventive measures and repair costs for exhaust guidance equipment and exhaust guidance system passages. , labor costs are required, and continuous transportation equipment between each facility is also required.
また、混練された原料は造粒機（パン造粒の場合は連続
運転）へ輸送されるが、輸送量が一定でないとパン内の
運動が崩れ、不良品が排出される。In addition, the kneaded raw materials are transported to a granulator (continuous operation in the case of bread granulation), but if the amount of transport is not constant, the movement within the bread will be disrupted and defective products will be discharged.
また、水スプレ位置、スプレ量の監視が必要であった。Additionally, it was necessary to monitor the water spray position and amount.
この発明は、上記のような実情に鑑みて、造粒が合理的
になされるために、その前工程として乾燥と粉砕の工程
を省略でき、一つのパン内において混合・粉砕・造粒の
工程を一挙になし得る貝化石等の粗管肥料基材の粒状化
方法を提供することを目的としたものである。In view of the above-mentioned circumstances, this invention enables granulation to be performed rationally, so that the drying and pulverizing steps can be omitted as pre-processes, and the mixing, pulverizing, and granulating steps can be performed in one pan. The purpose of this invention is to provide a method for granulating coarse tube fertilizer base materials such as shellfish fossils, which can accomplish the following in one step.
上記の目的を達成するためのこの発明の構成は。 The structure of this invention is to achieve the above object.
基材を粗砕する工程の次に、乾燥と粉砕の工程を省略し
、粗砕した基材をパン内に副資材と結合材と共に混入し
、パン内において逆流式高速混合により混合・粉砕・造
粒することをその要旨とする。Next to the step of coarsely crushing the base material, the drying and crushing steps are omitted, and the coarsely crushed base material is mixed into a pan together with auxiliary materials and binding materials, and then mixed, crushed, and mixed by high-speed backflow mixing in the pan. The gist is to granulate.
上記の構成によれば、基材を粗砕しただけで副資材や結
合材と共にパンに投入し、パン内において直ちに粉砕す
るが、その粉砕が強力な逆流式高速混合によるので、乾
燥がなされていなくても、所望の形態に粉砕や造粒が可
能であり、基材に含まれていた水分が却って造粒のため
に利用されるため、造粒中に水の供給が不要であり、必
要としても僅少で足りる。According to the above configuration, the base material is simply crushed and put into a pan together with auxiliary materials and binding materials, and is immediately crushed in the pan, but since the crushing is performed by powerful backflow high-speed mixing, drying is not performed. It is possible to crush and granulate into the desired form even without water, and since the water contained in the base material is instead used for granulation, there is no need to supply water during granulation. However, a small amount is enough.
逆流式高速混合は、パン内においてその中心に対して偏
心して設けられた撹拌工具がパンと逆方向に回転するの
で、基材が強力に破砕して粉体化される。また、工具の
形状によっては原料が躍動し、躍動により互いに摩擦し
ながら粒状化する。In the backflow type high-speed mixing, a stirring tool installed eccentrically with respect to the center of the pan rotates in the opposite direction to the pan, so that the base material is strongly crushed and powdered. Also, depending on the shape of the tool, the raw materials move, and the movement causes them to rub against each other and become granulated.
副資材の混入は製造目的の製品により計算値子αの添加
でよい。また、肥料には水中崩壊性テストがあるが、こ
れに対しては分散促進材として塩化物系のものを１．０
％前後添加すればよい。育苗床上においては、近年軽量
粒状品が要望されるが、嵩比重の小さいものを副資材と
して添加すればその要望に応えることができる。The mixing of auxiliary materials may be done by adding a calculated value α depending on the product to be manufactured. In addition, there is a water disintegration test for fertilizers, and for this test, a chloride-based dispersion promoter with a 1.0
It is sufficient to add around %. In recent years, there has been a demand for lightweight granular products for use on seedling beds, and this demand can be met by adding products with low bulk specific gravity as auxiliary materials.
粒状化促進材については、対象作物或は使用目的により
粉体または液体のものを選択的に添加する。粉体と液体
とのいずれの場合も、基材に対して１．５％以内の添加
量で足りる。Regarding the granulation accelerator, powder or liquid is selectively added depending on the target crop or purpose of use. In both cases of powder and liquid, it is sufficient to add the amount within 1.5% based on the base material.
また、最近ではゴルフ場向けの目上として着色粒状品が
要望されるが、顔料を添加すればその要望に応えること
ができる。Furthermore, recently there has been a demand for colored granular products for use in golf courses, and this demand can be met by adding pigments.
次に、この発明の実施例を図面に基づいて説明する。 Next, embodiments of the present invention will be described based on the drawings.
原材料およびその使用割合は次の通りである。The raw materials and their usage ratios are as follows.
（原材料） （使用割合）
基材 貝化石 １００副資材
水酸化苦土肥料 ８．８結合材（粒状
化促進材）ベントナイト １．０分散促進材
塩化前垂 １．５貝化石はローラ間に通すこ
とにより粗く粉砕する。しかしこれは他の手段、例えば
ハンマーで叩打する方法等によってもよい。このように
して粗砕した材料は、副資材や結合材、分散促進材と共
に計量し、次工程の逆流式高速混合工程に移行する。そ
の工程には商品名でアイリッヒ逆流式高速混合機（ドイ
ツ、アイリッヒ社製、日本アイリッヒ株式会社販売）と
称される装置（以下単に混合機と言う）を使用した。(Raw materials) (Usage ratio) Base material Fossil shell 100 Auxiliary materials Magnesium hydroxide fertilizer 8.8 Binder (granulation accelerator) Bentonite 1.0 Dispersion accelerator
Chloride apron 1.5 The shell fossils are coarsely crushed by passing them between rollers. However, this may also be done by other means, such as by hitting with a hammer. The thus coarsely crushed material is weighed together with auxiliary materials, binders, and dispersion promoters, and then transferred to the next step, a backflow type high-speed mixing step. In this process, an apparatus (hereinafter simply referred to as the mixer) called the Eirich backflow type high speed mixer (manufactured by Eirich Co., Ltd., Germany, sold by Eirich Japan Co., Ltd.) was used.
この混合機は、逆流原理に基づくもので、原料を入れた
パン１が時計方向に回転し、その中でパン中心に対して
偏心して取り付けられた撹拌工具２の混合羽根３にはす
くい角が付けられており、撹拌工具２が原料を跳ね上げ
ながら、パン１の中を相対的に円軌道を描いて回転する
ので、原料に万遍なく水平、垂直の流れが起きる。また
、パン１周辺の原料は、固定されたスクレーパによって
再び混合領域に戻される。This mixer is based on the backflow principle, in which a pan 1 containing raw materials rotates clockwise, and a mixing blade 3 of a stirring tool 2 mounted eccentrically with respect to the center of the pan has a rake angle. Since the stirring tool 2 rotates relatively in a circular orbit inside the pan 1 while throwing up the raw material, horizontal and vertical flows occur evenly in the raw material. Further, the raw materials around the pan 1 are returned to the mixing area by a fixed scraper.
このような機構に加えて、高速アジテータ５を導入でき
る。この高速アジテータ５は、パン１の中に取り付けら
れ、高速で回転することにより、打撃、摩擦の作用を発
揮する。また回転数、処理条件等を設定することにより
、造粒効果を持たせることができる。この造粒の特徴は
、粒子がほぼ均一で密度が高いことである。In addition to such a mechanism, a high speed agitator 5 can be introduced. This high-speed agitator 5 is installed in the pan 1 and rotates at high speed to exert impact and friction effects. Further, by setting the rotation speed, processing conditions, etc., a granulation effect can be imparted. The characteristics of this granulation are that the particles are almost uniform and dense.
液体およびガスは、パン１の中に導かれるパイプ、ある
いはスプレーノズルによって供給され、蒸気の吹き込み
は混合層の中に差し込まれた蒸気噴射管によって行なわ
れる。The liquid and gas are supplied by pipes or spray nozzles led into the pan 1, and the steam injection is carried out by a steam injection tube inserted into the mixing layer.
また、原料の供給は上部から、排出は下部中央から行な
われる。Further, raw materials are supplied from the top and discharged from the center of the bottom.
以上のように、この混合機は、種々の原料の加工に適し
、その均質化、混練、粉砕、はぐし活性化、調湿、造粒
という多機能を有している。この優れた機能を発揮でき
る理由は、通常化投入動力が１〜４ ＫＷ／１００ Ｑ
に対し、独特の工具の選択により１０〜２９ＫＷ／１０
０ Ｑまで高め、強力混合をなし得るからである。強力
混合の利点としては単位設備コスト或は据付面積当りの
処理量が大きいことが挙げられる。さらに、この混合機
によれば１次のような利点がある。As described above, this mixer is suitable for processing various raw materials, and has multiple functions such as homogenization, kneading, pulverization, loosening activation, humidity control, and granulation. The reason why this excellent function can be demonstrated is that the normal input power is 1 to 4 KW/100 Q.
10~29KW/10 due to unique tool selection
This is because it is possible to increase the temperature to 0 Q and achieve strong mixing. The advantage of intensive mixing is that the throughput per unit equipment cost or installation area is large. Furthermore, this mixer has the following advantages.
１）装置において工具の調整によりライナー、スフレバ
ーの摩耗が小さい。1) Wear of the liner and souffle bar is reduced by adjusting the tools in the equipment.
２）パン内は高速回転により打撃・摩擦作用により飛散
・流動し位置変換が活発であることから混合効果が向上
する。2) The high-speed rotation inside the pan causes the particles to scatter and flow due to impact and friction, resulting in active position changes, which improves the mixing effect.
３）従来困難であった顔料・固着剤等の添加も分塊・分
解し均一に混合される。3) Addition of pigments, fixing agents, etc., which was difficult in the past, can be done through agglomeration and decomposition, allowing for uniform mixing.
４）工具の種類、回転数処理条件等の設定により造粒（
核、種子）効果を持たせる。そのため粒状品ははゾ均一
で密度が高い。4) Granulation (
(nucleus, seed) effect. Therefore, granular products are highly uniform and dense.
５）装置はコンパクトに出来ており、作業環境が良好で
あり、またタイマー設定で自動化も可能である。5) The device is compact, provides a good working environment, and can be automated by setting a timer.
６）補修費も僅少で済む。6) Repair costs are also minimal.
そこで、混合機に粗砕された貝化石を副資材と結合材と
共に投入すると、混合・粉砕・造粒が行われるので、次
にパン１から排出した粒状の貝化石肥料を乾燥し、分級
することによって製品化する。Therefore, when the coarsely crushed shellfish fossils are put into the mixer together with auxiliary materials and binding materials, mixing, crushing, and granulation are performed.Then, the granular shellfish fossil fertilizer discharged from pan 1 is dried and classified. commercialize it by doing so.
混合機においては、バッチ方式のため、条件設定により
最良の運転状態が得られ、不良粒状品の排出がない。し
かも、貝化石には１０〜２０％の水分が含まれているが
、これはそのまま造粒の必要水分に利用されるので、造
粒時に水の補給は不要となり、必要としても僅少で足り
る。この点については、皿型造粒法においては、水の散
布のための作業員を必要としたが、その作業員は不要と
なる。Since the mixer is a batch system, the best operating conditions can be obtained by setting the conditions, and there is no discharge of defective granules. Moreover, fossil shells contain 10 to 20% water, but this is used as is for the water required for granulation, so there is no need to replenish water during granulation, and even if it is necessary, only a small amount is sufficient. Regarding this point, the dish-type granulation method required a worker to spray water, but that worker is no longer required.
また、従来の造粒機には危険防止対策が必要であるが、
この混合機によれば、パンが密閉して運転されるため、
何ら危険がないことは勿論、騒音も少く原材料が飛散す
る不都合もない。In addition, conventional granulators require safety measures, but
According to this mixer, the bread is operated in a sealed manner, so
Of course, there is no danger, there is little noise, and there is no inconvenience of raw materials scattering.
以上説明したように、基材を粗砕する工程の次に、造粒
工程に至るまでの前処理としての乾燥と粉砕の工程が省
かれるため、乾燥や粉砕のための土地、設備投資、エネ
ルギー、補修費、監視要員が不要となり、乾燥は造粒後
の比較的簡単な工程で足り、しかも造粒前における乾燥
の省略は、原料中の水分を造粒に寄与させる結果となる
ため、粗管肥料基材の粒状化について巧みにコストダウ
ンを計り得たという優れた効果がある。As explained above, after the process of coarsely crushing the base material, the drying and crushing process as a pretreatment before the granulation process is omitted, so there is no need for land, equipment investment, or energy for drying or crushing. , repair costs and monitoring personnel are not required, and drying is a relatively simple process after granulation, and omitting drying before granulation causes moisture in the raw materials to contribute to granulation, resulting in coarse grains. This has the excellent effect of skillfully reducing the cost of granulating the tube fertilizer base material.
加えて騒音や危険が少なく安全且つ良好な環境で操業が
可能となるという効果もある。In addition, there is also the effect that operations can be performed in a safe and favorable environment with less noise and danger.
第１図は従来例を説明するチャート図、第２図はこの発
明の詳細な説明するチャート図、第３図および第４図は
この発明の実施に使用した逆流式高速混合機の縦断面図
および要部横断面図である。
１・・パン ２・・・撹拌工具 ３・・・混合羽根
５・・高速アジテータFig. 1 is a chart diagram explaining a conventional example, Fig. 2 is a chart diagram explaining the present invention in detail, and Figs. 3 and 4 are longitudinal sectional views of a backflow type high speed mixer used in carrying out the present invention. and a cross-sectional view of main parts. 1... Pan 2... Stirring tool 3... Mixing blade 5... High speed agitator
Claims (1)
略し、粗砕した基材をパン内に副資材と結合材と共に混
入し、パン内において逆流式高速混合により混合・粉砕
・造粒することを特徴とする貝化石等の粗骨肥料基材の
粒状化方法。1) Next to the step of coarsely crushing the base material, the drying and crushing steps are omitted, and the coarsely crushed base material is mixed into a pan together with auxiliary materials and binders, and mixed by high-speed backflow mixing in the pan. A method for granulating coarse bone fertilizer base materials such as shellfish fossils, which comprises crushing and granulating them.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63272790A JPH0723274B2 (en) | 1988-10-28 | 1988-10-28 | Granulation method for coarse bone fertilizer base materials such as fossil shells |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63272790A JPH0723274B2 (en) | 1988-10-28 | 1988-10-28 | Granulation method for coarse bone fertilizer base materials such as fossil shells |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02120288A true JPH02120288A (en) | 1990-05-08 |
| JPH0723274B2 JPH0723274B2 (en) | 1995-03-15 |
Family
ID=17518780
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63272790A Expired - Fee Related JPH0723274B2 (en) | 1988-10-28 | 1988-10-28 | Granulation method for coarse bone fertilizer base materials such as fossil shells |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0723274B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020000097A (en) * | 2000-06-21 | 2002-01-04 | 김명오 | A process of fertilizer a componet with powdered bones and phosphorus |
| KR100432418B1 (en) * | 2001-08-29 | 2004-05-22 | 정경자 | Manufacturing process of granule multinutrient fertilizer using crushed waste shells |
| DE10062598B4 (en) * | 2000-12-15 | 2010-12-23 | Basf Se | Process for the targeted agglomeration of fertilizers |
-
1988
- 1988-10-28 JP JP63272790A patent/JPH0723274B2/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20020000097A (en) * | 2000-06-21 | 2002-01-04 | 김명오 | A process of fertilizer a componet with powdered bones and phosphorus |
| DE10062598B4 (en) * | 2000-12-15 | 2010-12-23 | Basf Se | Process for the targeted agglomeration of fertilizers |
| KR100432418B1 (en) * | 2001-08-29 | 2004-05-22 | 정경자 | Manufacturing process of granule multinutrient fertilizer using crushed waste shells |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0723274B2 (en) | 1995-03-15 |
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