WO1999059932A1 - Cement grinder - Google Patents

Cement grinder Download PDF

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Publication number
WO1999059932A1
WO1999059932A1 PCT/JP1998/002238 JP9802238W WO9959932A1 WO 1999059932 A1 WO1999059932 A1 WO 1999059932A1 JP 9802238 W JP9802238 W JP 9802238W WO 9959932 A1 WO9959932 A1 WO 9959932A1
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WO
WIPO (PCT)
Prior art keywords
cement
grinding
raw material
gap
plate
Prior art date
Application number
PCT/JP1998/002238
Other languages
French (fr)
Japanese (ja)
Inventor
Hiromi Yamamoto
Original Assignee
Hiromi Yamamoto
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Hiromi Yamamoto filed Critical Hiromi Yamamoto
Priority to PCT/JP1998/002238 priority Critical patent/WO1999059932A1/en
Priority to AU74497/98A priority patent/AU7449798A/en
Publication of WO1999059932A1 publication Critical patent/WO1999059932A1/en

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C7/00Crushing or disintegrating by disc mills
    • B02C7/02Crushing or disintegrating by disc mills with coaxial discs
    • B02C7/08Crushing or disintegrating by disc mills with coaxial discs with vertical axis
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B02CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
    • B02CCRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
    • B02C7/00Crushing or disintegrating by disc mills
    • B02C7/11Details
    • B02C7/12Shape or construction of discs

Definitions

  • the present invention relates to a cement grinding apparatus used for grinding raw material cement in order to obtain ground cement used as a concrete material when producing highly fluid concrete.
  • cement used for fluid concrete for example, ordinary cement (Portland cement, etc.) is used alone as admixture (fly ash, blast furnace slag fine powder, limestone fine powder, silica fume, etc.).
  • admixture for example, two-component cements and three-component cements that are mixed or mixed with admixtures from the beginning. These admixtures have improved fluidity and are capable of producing concrete with high density and high durability.
  • the high-speed airflow impact device When supplied to the raw material cement colliding collision chamber, the high-speed airflow impact device scatters while rotating in the raw material culling collision chamber due to the rotation of the rotating plate and the blade attached thereto.
  • the blades were configured to repeatedly collide between the blades and a large number of grooves provided on the surface of the stay. Therefore, by using this apparatus, it was possible to obtain cement fine particles which became spherical due to the angular force of the outer peripheral surface being 5.
  • this high-speed airflow impact device has a structure in which the ring-shaped stay holds the ring-shaped collision chamber and surrounds the rotating plate. For this reason, it is necessary to machine the ring-shaped stator into an annular shape, which increases the size of the device and increases the manufacturing cost.
  • the raw material cement is scattered and made spherical by the impact of the collision between the groove and the blade, it is difficult to obtain a polishing action by rubbing of the raw material cement there. For this reason, the raw material cement must be scattered at a high speed and the processing time needs to be long, so that there has been a problem that working efficiency cannot be improved.
  • the present invention has been made to solve the above-mentioned conventional problems, and the raw cement is ground between a pair of grinding plates arranged axially facing each other.
  • the grinding cement has a simple structure, but is efficient, and the cement particles are rounded and miniaturized.
  • the purpose is to provide a cement grinding device that can be processed into a single piece. Disclosure of the invention
  • the rotating grinding plate connected to the rotary driving device and the fixed grinding plate fixed to the machine frame keep a gap therebetween in the axial direction of the rotating grinding plate.
  • a supply hole for the raw material cement communicating with the gap is formed in one of the grinding plates, and at least a protruding portion is provided on the facing surface of the rotary grinding plate.
  • the fixed grinding plate can also be provided with a protruding portion.
  • the rotary grinding plates connected to the rotary driving device are arranged so as to oppose each other in the axial direction of the rotary grinding plate so as to keep the gap so that the rotation direction is reversed.
  • a supply hole for the raw material cement communicating with the gap is formed in one of the milling plates, and a protruding portion is provided on at least one of the rotating milling plates in a facing surface. In this case, a projection can be provided on each of the rotary grinding plates.
  • the raw material cement is supplied from the supply hole while the rotary grinding plate is rotated by the rotary driving device.
  • the raw material cement flows into the gap, where it is swirled by the projections provided on the rotary milling plate, moves in the circumferential direction, and is ground by the centrifugal force while moving in the outer circumferential direction. That is, during this movement, the cement particles are polished by the rubbing of the cement particles due to the rotation of the crushing plate, and are crushed by the impact by colliding with the protrusions. It is discharged from the outer periphery of the gap as crushed cement.
  • the cement particles have rounded corners.
  • the cement particles are miniaturized by the angular force of the cement particles, and are further miniaturized by the removed corners and cracks of the cement particles. Therefore, since the cement particles are rounded, the fluidity can be improved by the bearing effect.
  • the particle diameter of the cement particles is reduced as a whole, the voids between the particles are reduced, and the actual volume ratio is improved. As a result, it is possible to reduce the unit water volume, improve the specificity of the concrete, and obtain a high-density, fine, highly durable concrete.
  • a pair of grinding plates are arranged to face each other in the axial direction.
  • a portland cement system containing a cement clinker having a specific surface area of more than 2000 cm 2 Zg ordinary portland cement, early-strength portland cement, ultra-high-strength portland cement, moderate heat Portland cement, including the sulfate resistance por Bok land cement
  • the specific surface area of 2 0 0 0 cm 2 / gl ⁇ mixed cementitious containing the cement clinker Lh blast furnace cement, fly ash cement, silica Special cement (including alumina cement and ultra-hard cement) can be used.
  • the ground cement obtained by grinding the raw material cement once or a plurality of times may be used alone, or a mixture of the above-mentioned cements may be used again as the raw material cement.
  • the raw material cement can be used after being heated to 150 ° C. to 140 ° C., and in this case, the grinding of the raw material cement is promoted, and efficient processing can be performed.
  • the orientation of the two grinding plates there are a mode in which the plates are vertically opposed, a mode in which the plates are horizontally opposed, and a mode in which the plates are obliquely arranged.
  • the gap formed between the two grinding plates may be formed in a flat shape, a conical shape, or a spherical shape.
  • an air blowing hole for blowing air into the gap is formed in one of the grinding plates.
  • the air blow hole may be used as a supply hole for raw cement, or may be formed on one of the grinding plates separately from the supply hole for raw cement.
  • the discharge amount can be adjusted by increasing or decreasing the blowing amount.
  • the protruding portion a mode in which this is a mesh body stretched on the opposing surface, a mode in which it is a number of protruding bodies protruding on the opposing surface, a combination of the net and the protruding body
  • the protrusions include protrusions or ridges, and combinations of protrusions and ridges.
  • the protruding portion includes a protruding portion formed such that the protruding height H is equal to or less than half (H ⁇ 2L) of the valley interval L between the protruding portions.
  • the projecting portion has a function of moving the raw material cement in the gap in the circumferential direction and a function of crushing the raw material cement by an impact caused by collision with the raw material cement. When the raw cement force is clogged in the valleys between the protrusions, the height of the protrusion decreases accordingly, and the effect of the protrusion decreases.
  • FIG. 1 is a schematic sectional view of a preferred cement grinding apparatus according to the present invention.
  • FIG. 2 is a plan view of a rotary grinding plate provided in the cement grinding device, and
  • FIG. 3 is an enlarged cross-sectional view showing a net as a projection provided in the rotary grinding plate.
  • FIGS. 4 and 5 are schematic cross-sectional views showing a rotary driving form of a grinding plate provided in a cement grinding apparatus.
  • FIGS. 6 and 7 are schematic cross-sectional views showing a facing arrangement form of the grinding plates.
  • Fig. 8 is a schematic sectional view showing the position of the supply holes provided in the grinding plate,
  • Figs. 9 to 11 are schematic sectional views showing the form of the gap formed between the grinding plates, and Figs.
  • FIGS. 13 and 13 are schematic cross-sectional views showing the configuration of the air blow holes provided in the grinding plate
  • Figs. 14 to 17 are the shapes of the protrusions provided on the opposing surface of the grinding plate.
  • FIGS. 18 to 23 show cross-sectional shapes of the protruding portions, and are cross-sectional explanatory diagrams showing the relationship between the protruding height and the valley interval between the protruding portions
  • FIGS. 24 and Fig. 25 shows the protrusion
  • FIG. 1 is a schematic sectional view of a cement grinding apparatus according to one embodiment of the present invention
  • FIG. 2 is a plan view of a rotary grinding plate provided in the cement grinding apparatus
  • FIG. It is an expanded sectional view of the protrusion provided in this rotary grinding plate.
  • This cement grinding device includes a fixed grinding plate 1 and a rotating grinding plate 2 that are arranged vertically and opposed to each other, and a gap 3 is formed between the grinding plates 1 and 2.
  • the fixed grinding plate 1 is made of metal (iron, iron, stainless steel, etc.), synthetic resin, ceramic, other materials having excellent wear resistance, and the like, and is formed in a circular shape. A cement supply hole is formed.
  • the fixed grinding plate 1 is fixed to the casing 4 via a machine frame 40.
  • the casing 4 is formed of stainless steel in a cylindrical shape, and is formed at its upper end with a loading hopper 41 s communicating with the supply hole 10 and at its lower end with a discharge square 42 force.
  • the rotary grinding plate 2 is formed in a circular shape with the same material as the fixed grinding plate 1, and a rotation driving device 20a is connected to a central portion of the lower surface thereof.
  • a rotary shaft 21 pivotally supported by a casing 4 is connected to the center of the lower surface of the rotary grinding plate 2, and a pulley 22 is attached to the rotary shaft 21.
  • the belt 2 is wound around the belt 2 3 times 3 times, and the rotating force from a drive motor (not shown) is transmitted to the rotary grinding plate 2 via the rotating shaft 21.
  • the gap 3 is formed in a planar shape, and protruding edges 30 and 30 are protruded toward the gap 3 along the outer circumferences of the grinding plates 1 and 2.
  • the protruding edge 30 is not always necessary, and the protruding edge 30 is
  • reticulated bodies 50 and 50 are respectively provided as projections.
  • the mesh 50 of the rotary milling plate 2 will be described.
  • a metal wire rod 51 having a circular cross section is woven in a lattice shape. It is manufactured separately and attached to the opposing surface 24 of the rotary grinding plate 2 by welding.
  • this net-like body 50 has a protruding portion formed such that the protruding height H of the metal wire 51 constituting the net is less than half (H ⁇ 2 L) of the valley interval L between the metal wires 51. Contains.
  • the mesh 50 of the fixed grinding plate 1 is formed in the same manner. It is sufficient that the mesh body 50 (projection) is provided at least on the facing surface 24 of the rotary grinding plate 2.
  • the raw cement is supplied from the supply hole 10 while the rotary grinding plate 2 is rotated by the rotary drive device 20a.
  • This raw material cement flows into the gap 3, where it is swirled by the mesh 50 provided on the rotary milling plate 2, moves in the circumferential direction, and is ground by the centrifugal force while moving in the outer circumferential direction. . That is, during this movement, the cement particles are polished by the rubbing of the cement particles due to the rotation of the rotary grinding plate 2, and are crushed by the impact by colliding with the nets 50, 50.
  • the milled raw cement is discharged from the outer periphery of the gap 3 as milled cement.
  • the raw material cement supplied from the supply hole 10 flows into the gap 3, is ground there, and then discharged from the outer periphery of the gap 3. Milled cement can be produced continuously.
  • the protruding edges 30, 30 are protruded along the outer peripheries of the both grinding plates 1, 2, the outlet of the cement is narrow. As a result, the amount of cement discharged is suppressed, so that the raw material cement
  • the mesh 50 of the rotary milling plate 2 has a function of moving the raw material cement in the circumferential direction in the gap 3, and the meshes 50, 50 of the milling plates 1, 2
  • the impact of the collision with the raw material cement has the effect of crushing the raw material cement.
  • the protruding height becomes lower.
  • the effect of the network 50 is reduced. Therefore, in order to prevent the raw material cement from clogging the valley between the metal wires 51 and 51 as much as possible, the relationship between the valley interval L and the protrusion height H should be H ⁇ 2L.
  • the present applicant shows an example of a test result when a fluid cement is manufactured using this cement grinding device.
  • Ordinary Portland cement was used as the raw material cement, and the diameter of fixed milling plate 1 and rotating milling plate 2 was set to 80 cm, and rotating milling plate 2 was rotated at 300 O rpm to produce milled cement. .
  • the concrete using the raw cement was 15.5 cm.
  • concrete with milled cement was 18.5 cm.
  • the slump value was 20 cm. If the temperature is less than 15 (TC, the grinding process cannot be accelerated, and if the temperature exceeds 140 ° C, the raw material cement will be melted. C ⁇ 140 ° C. As is evident from the test results, it is necessary to grind the raw material cement.
  • Fig. 4 shows the case where the rotating grinding plate 2 is placed on the upper side and the fixed grinding plate 1 is placed on the lower side and opposed to each other.
  • Drive 2 ⁇ b is connected.
  • a cylindrical rotary shaft 25 supported by a casing is connected to the center of the upper surface of the rotary grinding plate 2, and a pulley 26 force is attached to the cylindrical rotary shaft 25.
  • the belt 27 is rotated by the pulley 26, and the rotational force of a drive motor (not shown) is transmitted to the rotary grinding plate 2 via the cylindrical rotary shaft 25. It has become.
  • a supply hole 28 communicating with the inside of the cylindrical rotary shaft 25 is formed at the center of the rotary milling plate 2, and the raw material cement passes through the inside of the cylindrical rotary shaft 25 and is supplied with the supply hole 28. From the gap 3 to the gap 3.
  • Fig. 5 shows a case where the rotary grinding plates 2, 2 connected to the rotary drive units 20a, 20b are opposed to each other while maintaining a gap 3 so that the rotation direction is reversed.
  • a supply hole 28 for the raw material cement communicating with the gap 3 is formed in the upper rotary milling plate 2.
  • the protruding portion may be provided on each of the rotary grinding plates 2, 2, or may be provided on at least one of the rotary grinding plates 2.
  • a force indicating a case where the fixed milling plate 1 and the rotary milling plate 2 are arranged opposite to each other is used to connect the rotary milling plates 2 and 2 as shown in FIG. It can also be applied to the case of facing.
  • a cement grinding apparatus may be configured by combining the following embodiments.
  • Fig. 6 shows a case where both grinding plates 1 and 2 are arranged to face each other in the left and right direction
  • Fig. 7 shows a case where both grinding plates 1 and 2 are arranged to face each other diagonally.
  • the position of the feed hole 10 for the raw cement may be formed at a position eccentric from the center of the milling plate 1 as shown in FIG.
  • FIG. 9 shows a case where the gap 3 is formed in an upward conical shape
  • FIG. 10 shows a case where the gap 3 is formed in an upward spherical shape.
  • the gap 3 may be formed in a downward conical shape or a downward spherical shape.
  • Fig. 11 shows the case where the gap 3 is gradually narrowed from the center to the outer periphery.
  • the opposing surface 11 of the fixed grinding plate 1 is formed as a flat surface, and the rotary grinding is performed.
  • the opposing surface 24 of the crushing plate 2 is formed as an inclined surface that gradually becomes deeper from the outer periphery toward the center.
  • the opposed surface 11 of the fixed grinding plate 1 may be formed as an inclined surface
  • the opposed surface 24 of the rotary grinding plate 2 may be formed as a flat surface.
  • the opposing surfaces 11 and 24 of the plate 1 and the rotary milling plate 2 may be formed on inclined surfaces, respectively.
  • Fig. 12 shows the case where the supply hole 10 formed in the upper fixed grinding plate 1 is also used as the air blowing hole 6 ⁇
  • Fig. 13 shows the case where the upper rotating grinding plate 2 is formed.
  • This shows a case where an air blow hole 61 is formed in the lower fixed grinding plate 1 separately from the feed hole 28 for the raw material cement.
  • the air blowing hole 61 has its outlet formed by a large number of small holes 62, and the small holes 62 are opened obliquely from the center toward the outer periphery.
  • reference numeral 63 denotes an air introducing cylinder.
  • FIG. 14 Next, the protrusion will be described with reference to FIGS. 14 to 25.
  • Fig. 14 shows a number of protrusions with protrusions projecting from the facing surface 24.
  • the planar shape of the projection 52 can be arbitrarily determined, such as a circle, a square, or a cross.
  • FIG. 15 shows a case where the projecting portion is formed by a large number of projecting ridges 53 which are a large number of projecting bodies projecting radially from the facing surface 24.
  • the planar shape of the ridge 53 is formed in an arc shape in which the surface of the rotary grinding plate 2 in the rotation direction (the direction of the arrow) is concave.
  • the plane shape of the ridge 53 can be arbitrarily determined, such as a force, a linear shape, a wavy shape, a net shape, a spider web shape, or the like.
  • FIG. 16 shows a case where the projections are formed by a combination of a number of projections 52 projecting from the facing surface 24 and a number of projections 53 formed in a spider web shape.
  • FIG. 17 shows a case where the protruding portion is formed by a combination of the net 50, the protrusion 52, and the protrusion 53.
  • a rectangular cross-section as shown in Fig. 18, a triangular cross-section as shown in Fig. 19, a circular cross-section as shown in Fig. 20, and a trapezoidal cross-section as shown in Fig. 21 may be formed in a semicircle or the like.
  • the cross-sectional shape of the protruding portion 5 may be the same circular cross-section, and the size may be different. Alternatively, as shown in FIG. Different cross-sectional shapes may be combined, such as combining cross-sections.
  • the valley interval L is The distance from the upper edge 54 of the protruding portion 5.
  • the protruding portion has a triangular cross section or a circular cross section as shown in FIGS. 19 and 20, the top of the protruding portion 5 The distance from Also, as shown in Fig. 22 and Fig. 23, when the protruding height force s is different, it is expressed by the relational expression with the valley interval L (H ⁇ 2L)
  • the protrusion height H refers to the protrusion height of the lower protrusion 5a.
  • the protruding height is twice as large as that of the metal wire 5] due to the overlap of the metal wires 51.
  • the protruding height is different between the intersection and the portion other than the intersection.
  • the protrusion height H refers to the height of the protrusion having the lower height.
  • FIGS. 24 and 25 show examples of the case where H> 2 L in the relationship between the protrusion height H and the valley interval L.
  • the valley becomes narrower, which causes a problem that the raw material cement tends to cause clogging.
  • the protruding portion in which the relationship between the protruding height H and the valley interval L satisfies H ⁇ 2 includes 20% or more of the entire protruding portion.
  • the force formed when including 80% lil ⁇ of the entire protruding portion is at least 20% or more of the entire protruding portion. A crushing effect is obtained.
  • the material of the attrition plate, the diameter of the attrition plate, the rotation speed, the clearance of the gap, and the like are appropriately determined according to the degree of attrition, the throughput, and the like.
  • the rotary drive device may have any structure as long as the rotary force from the drive source can be transmitted to the grinding plate by a transmission means such as a belt, a chain, and a gear.
  • the ground cement thus processed is used as a raw material for concrete buildings in the construction industry, concrete structures in the civil engineering industry, and other concrete products.

Abstract

A cement grinder used for grinding raw cement so as to obtain ground cement used as a material for the production of concrete of a high fluidity, comprising a rotary grinding plate (2) joined to a rotary driving unit (21a), a stationary grinding plate (1) fixed to a machine frame (40) and opposed to the rotary grinding plate (2) in the axial direction thereof with a clearance (3) kept therebetween, a raw cement supply port (10) formed in one (stationary grinding plate (1)) of the grinding plates and communicating with the clearance (3), and protrusions (reticulum (50)) provided on an opposed surface (24) of at least the rotary grinding plate (2), wherein the raw cement supplied to the clearance (3) is ground by the relative frictional movements of the grinding plates and pulverized by the collision of raw cement particles, thus enabling the cement grinder of a simple construction to carry out the rounding of the cement particles and the manufacturing of micronized ground cement.

Description

セメント摩碎装置 Cement grinding equipment
技術分野 Technical field
本発明は、 流動性が高いコンクリートを製造する際に、 そのコンク リ一卜材料として使用される摩砕セメントを得るために、 原料セメント を摩砕するのに用いられるセメン卜摩砕装置に関する。 背景技術  TECHNICAL FIELD The present invention relates to a cement grinding apparatus used for grinding raw material cement in order to obtain ground cement used as a concrete material when producing highly fluid concrete. Background art
流動性が高いコンクリートは、 打ち込み作業に際し、 その流動性に よつて型枠の隅々にまで容易かつ確実にコンクリートを充填できること から、 打ち込み作業の簡略化、 コンクリー卜構造物の信頼性の向上など 多くの利点があり、 今後の需要がますます増大すると予想される。 従来、 流動性力 いコンクリー卜に使用されるセメントとしては、 例 えば、 通常のセメント (ポルトランドセメント等) に単独で混和材 (フ ライアッシュ、 高炉スラグ微粉末、 石灰石微粉末、 シリカフューム等) を混合するか、 あるいは始めから混和材が混合されている二成分セメン 卜や三成分セメント力 S知られている。 そして、 これらの混和材によって 流動性が向上すると共に、 高密度、 高耐久性のコンクリートが得られて いる。  Concrete with high fluidity can be easily and reliably filled into every corner of the formwork due to the fluidity of the concrete at the time of placing work, so simplification of the placing work and improvement of the reliability of concrete structures, etc. It has many advantages and is expected to increase in demand in the future. Conventionally, as cement used for fluid concrete, for example, ordinary cement (Portland cement, etc.) is used alone as admixture (fly ash, blast furnace slag fine powder, limestone fine powder, silica fume, etc.). Known are two-component cements and three-component cements that are mixed or mixed with admixtures from the beginning. These admixtures have improved fluidity and are capable of producing concrete with high density and high durability.
このように、 従来では、 流動性力 いコンクリ一卜を製造するには、 混和材を混合することが不可欠であるため、 価格面や混合手間等の面で 不利になるという問題があった。  As described above, conventionally, in order to produce a concrete having fluidity, it is indispensable to mix an admixture, so that there has been a problem in that it is disadvantageous in terms of price and mixing time.
この問題に対処するものとして、 例えば、 日本国公開特許公報 (特開 平 2— 3 1 1 3 3 8号) に開示されているように、 原料セメントを球状 に微小ィヒし、 そのべァリング効果によって流動性を高めることに着目し  To cope with this problem, for example, as disclosed in Japanese Patent Application Laid-Open Publication No. Hei 2-3-111338, the raw material cement is finely divided into spherical particles, and the resulting cement is baked. Focus on increasing liquidity through effects
差替え用紙 (規則 26) た高速気流中衝撃装置 「商品名 ナラーハイプリタイザ一」 (株式会社 奈良機械製作所製) が提案されている。 Replacement form (Rule 26) A high-speed airflow impact device “Nara High Pretizer I” (produced by Nara Machinery Co., Ltd.) has been proposed.
この高速気流中衝撃装置は、 原料セメントカ リング状衝突室に供給さ れると、 回転板とこれに取り付けられたブレードの回転により、 原料セ メン卜カ リング状衝突室内を回転しながら飛散し、 リング状ステ一夕の 表面に設けられた多数の溝と前記ブレードとの間で衝突を繰り返すよう に構成されていた。 従って、 この装置を用いれば、 外周面の角力 ¾5れて 球状となったセメン卜微小粒子を得ることができるものであった。 しかしながら、 この高速気流中衝撃装置は、 リング状ステ一夕がリン グ状衝突室を保持して回転板を囲む構造となっている。 このため、 リン グ状ステータを環状に加工する必要があり、 その分だけ装置が大掛かり になり、 製作コスト力 くなる。 又、 原料セメントを飛散させ、 溝とブ レードとの間の衝突による衝撃で球状化させるため、 そこには原料セメ ン卜の擦れ合いによる研摩作用が得られ難い。 このため、 原料セメント を高速で飛散させると共に加工時間を長くする必要が生じ、 作業能率を 向上することができないという問題があつた。  When supplied to the raw material cement colliding collision chamber, the high-speed airflow impact device scatters while rotating in the raw material culling collision chamber due to the rotation of the rotating plate and the blade attached thereto. The blades were configured to repeatedly collide between the blades and a large number of grooves provided on the surface of the stay. Therefore, by using this apparatus, it was possible to obtain cement fine particles which became spherical due to the angular force of the outer peripheral surface being 5. However, this high-speed airflow impact device has a structure in which the ring-shaped stay holds the ring-shaped collision chamber and surrounds the rotating plate. For this reason, it is necessary to machine the ring-shaped stator into an annular shape, which increases the size of the device and increases the manufacturing cost. Also, since the raw material cement is scattered and made spherical by the impact of the collision between the groove and the blade, it is difficult to obtain a polishing action by rubbing of the raw material cement there. For this reason, the raw material cement must be scattered at a high speed and the processing time needs to be long, so that there has been a problem that working efficiency cannot be improved.
本発明は、 上述のような従来の問題を解決するためになされたもの で、 軸方向に対向配置した 1対の摩碎板の間で原料セメントを摩碎加工 するようにした。 即ち、 原料セメントの擦れ合いによる研摩作用と、 原 料セメントの衝突による破砕作用を併せ行わせることにより、 簡単な構 造でありながら効率よく、 セメント粒子が丸みを帯びると共に微小化し た摩碎セメン卜に加工できるようにしたセメント摩砕装置を提供するこ とを目的としている。 発明の開示  SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned conventional problems, and the raw cement is ground between a pair of grinding plates arranged axially facing each other. In other words, by combining the grinding action of the raw cement with the rubbing action of the raw cement and the crushing action of the raw cement, the grinding cement has a simple structure, but is efficient, and the cement particles are rounded and miniaturized. The purpose is to provide a cement grinding device that can be processed into a single piece. Disclosure of the invention
本発明のセメント摩砕装置は、 回転駆動装置に連結された回転摩砕板 と機枠に固定された固定摩碎板とが間隙を保持して回転摩碎板の軸方向  In the cement grinding apparatus of the present invention, the rotating grinding plate connected to the rotary driving device and the fixed grinding plate fixed to the machine frame keep a gap therebetween in the axial direction of the rotating grinding plate.
差替え用紙 (規則 26) に対向配置され、 前記間隙に連通する原料セメン卜の供給穴が一方の摩 砕板に形成され、 少なくとも回転摩砕板の対向面に突出部が設けられて いる。 この場合、 固定摩砕板にも突出部を設けることができる。 Replacement form (Rule 26) A supply hole for the raw material cement communicating with the gap is formed in one of the grinding plates, and at least a protruding portion is provided on the facing surface of the rotary grinding plate. In this case, the fixed grinding plate can also be provided with a protruding portion.
又、 本発明のセメント摩砕装置は、 回転方向が逆になるように回転駆 動装置に連結された回転摩砕板同士が間隙を保持して回転摩砕板の軸方 向に対向配置され、 前記間隙に連通する原料セメン卜の供給穴が一方の 摩砕板に形成され、 少なくとも一方の回転摩碎板の対向面に突出部が設 けられている。 この場合、 両回転摩砕板にそれぞれ突出部を設けること ができる。  Further, in the cement grinding apparatus of the present invention, the rotary grinding plates connected to the rotary driving device are arranged so as to oppose each other in the axial direction of the rotary grinding plate so as to keep the gap so that the rotation direction is reversed. A supply hole for the raw material cement communicating with the gap is formed in one of the milling plates, and a protruding portion is provided on at least one of the rotating milling plates in a facing surface. In this case, a projection can be provided on each of the rotary grinding plates.
従って、 このセメント摩砕装置を使用するに際しては、 回転摩砕板を 回転駆動装置によって回転させながら、 供給穴から原料セメン卜を投入 する。 この原料セメントは間隙に流入し、 ここで回転摩砕板に設けられ た突出部により連れ回されて円周方向へ移動すると共に遠心力によって 外周方向に移動しながら摩砕される。 即ち、 この移動中に摩碎板の回転 によるセメント粒子同士の擦れ合いによって研摩されると共に、 突出部 に衝突することによる衝撃によつて破砕され、 この摩碎加工された原料 セメン卜は、 摩砕セメン卜となって間隙の外周から排出される。  Therefore, when using this cement grinding device, the raw material cement is supplied from the supply hole while the rotary grinding plate is rotated by the rotary driving device. The raw material cement flows into the gap, where it is swirled by the projections provided on the rotary milling plate, moves in the circumferential direction, and is ground by the centrifugal force while moving in the outer circumferential direction. That is, during this movement, the cement particles are polished by the rubbing of the cement particles due to the rotation of the crushing plate, and are crushed by the impact by colliding with the protrusions. It is discharged from the outer periphery of the gap as crushed cement.
このようにして得られた摩砕セメントは、 セメン卜粒子の角が取れて 丸みを帯びることになる。 又、 セメント粒子の角力 れることによる細 粒化によって微小化すると共に、 取れた角やセメント粒子の割れによつ てさらに微小化される。 従って、 セメント粒子が丸みを帯びているた め、 ベアリング効果により流動性の向上を図ることができる。 又、 全体 的にセメント粒子の粒径が小さくなるために粒子間空隙が小さくなり、 実積率が向上する。 この結果、 単位水量を減少することができ、 コンク リートのヮ一力ピリティーが向上すると共に、 高密度できめが細かく、 高耐久性のコンクリートを得ることができる。  In the milled cement thus obtained, the cement particles have rounded corners. In addition, the cement particles are miniaturized by the angular force of the cement particles, and are further miniaturized by the removed corners and cracks of the cement particles. Therefore, since the cement particles are rounded, the fluidity can be improved by the bearing effect. In addition, since the particle diameter of the cement particles is reduced as a whole, the voids between the particles are reduced, and the actual volume ratio is improved. As a result, it is possible to reduce the unit water volume, improve the specificity of the concrete, and obtain a high-density, fine, highly durable concrete.
又、 本発明では、 1対の摩砕板を軸方向に対向配置したため、 構造が  In addition, in the present invention, a pair of grinding plates are arranged to face each other in the axial direction.
差替え用紙 (規則 26) 簡単でありながら、 原料セメントの擦れ合いによる研摩作用と、 原料セ メン卜の衝突による破砕作用を併せ行わせることができ、 セメント粒子 が丸みを帯びると共に微小化した摩砕セメン卜に効率よく加工すること ができる。 Replacement form (Rule 26) Although it is simple, it can combine the grinding action due to the rubbing of the raw material cement and the crushing action due to the collision of the raw material cement, efficiently processing cement particles that are rounded and miniaturized. can do.
ここで、 原料セメントとしては、 比表面積 2 0 0 0 c m 2 Z g以上の セメントクリンカを含んでいるポル卜ランドセメン卜系 (普通ポルトラ ンドセメント、 早強ポルトランドセメント、 超早強ポル卜ランドセメン 卜、 中庸熱ポルトランドセメント、 耐硫酸塩ポル卜ランドセメントを含 む) 、 又、 比表面積 2 0 0 0 c m 2 / gl^Lhのセメントクリンカを含ん でいる混合セメント系 (高炉セメント、 フライアッシュセメント、 シリ 力セメントを含む) 、 それに特殊セメント系 (アルミナセメント、 超速 硬セメントを含む) 等を使用することができる。 又、 原料セメントを 1回あるいは複数回摩砕加工した摩砕セメントを単独で、 あるいは前記 した各セメン卜に混合したものを再び原料セメン卜として用いてもよ い。 又、 原料セメントを 1 5 0 °C~ 1 4 0 0 °Cに加熱して使用すること もでき、 この場合、 原料セメントの摩砕が促進され、 効率のよい加工が できる。 Here, as the raw material cement, a portland cement system containing a cement clinker having a specific surface area of more than 2000 cm 2 Zg (ordinary portland cement, early-strength portland cement, ultra-high-strength portland cement, moderate heat Portland cement, including the sulfate resistance por Bok land cement), in addition, the specific surface area of 2 0 0 0 cm 2 / gl ^ mixed cementitious containing the cement clinker Lh (blast furnace cement, fly ash cement, silica Special cement (including alumina cement and ultra-hard cement) can be used. Further, the ground cement obtained by grinding the raw material cement once or a plurality of times may be used alone, or a mixture of the above-mentioned cements may be used again as the raw material cement. In addition, the raw material cement can be used after being heated to 150 ° C. to 140 ° C., and in this case, the grinding of the raw material cement is promoted, and efficient processing can be performed.
又、 両摩砕板の向きについては、 上下方向に対向配置する態様、 左右 方向に対向配置する態様、 斜め方向に対向配置する態様がある。  As for the orientation of the two grinding plates, there are a mode in which the plates are vertically opposed, a mode in which the plates are horizontally opposed, and a mode in which the plates are obliquely arranged.
又、 原料セメントの供給穴の位置について、 摩砕板の中心に形成され ている態、様、 摩砕板の中心から偏心した位置に形成されている態様があ る。  In addition, there is a mode in which the position of the supply hole for the raw material cement is formed at the center of the milling plate, or in a position eccentric from the center of the milling plate.
又、 両摩砕板の間に形成された間隙については、 平面状に形成する態 様、 円錐状に形成する態様、 球面状に形成する態様がある。  The gap formed between the two grinding plates may be formed in a flat shape, a conical shape, or a spherical shape.
又、 間隙が中央部から外周部に向けて次第に狭幅に形成されている態 様と、 少なくとも一方の摩砕板の外周に沿って突出縁が間隙に向けて突 設されている態様がある。 この突出縁は、 両摩砕板に設けることができ  In addition, there is a mode in which the gap is gradually narrowed from the central portion to the outer peripheral portion, and a mode in which a protruding edge projects toward the gap along the outer circumference of at least one of the grinding plates. . This protruding edge can be provided on both grinding plates
差替え用紙 (規則 26) る。 回転している摩碎板の周速及び遠心力は外周側ほど大きいため、 間 隙に流入した原料セメントは、 外周側に移動するにつれ移動速度が速く なり、 それだけ原料セメン卜力 ^疎になってセメント粒子同士の擦れ合い が薄くなる。 これに対し、 間隙を中央部から外周部に向けて次第に狭幅 に形成し、 あるいは摩砕板の外周に沿って突出縁を突設すると、 セメン 卜の出口が狭くなるためセメン卜の排出量が抑制される。 これにより原 料セメントが間隙を密な; I犬態で移動することになるし、 間隙に滞留する 時間が長くなる。 従って、 セメント粒子同士の擦れ合いが厚くなると共 に、 擦れ合いの時間が長くなり、 この結果、 原料セメントを効率的かつ 効果的に摩砕加工することができる。 Replacement form (Rule 26) You. Since the peripheral speed and centrifugal force of the rotating milling plate are higher on the outer peripheral side, the moving speed of the raw material cement flowing into the gap increases as it moves to the outer peripheral side, and the raw material cement power becomes less sparse. This reduces the friction between the cement particles. On the other hand, if the gap is formed gradually narrower from the center to the outer periphery, or if a protruding edge is protruded along the outer periphery of the grinding plate, the outlet of the cement becomes narrower, so that the amount of cement discharge is reduced. Is suppressed. This will cause the feed cement to move closer in the gap; I will move in a dog-like manner and will stay in the gap longer. Therefore, the rubbing between the cement particles becomes thicker and the rubbing time becomes longer. As a result, the raw material cement can be efficiently and effectively ground.
又、 間隙に空気を送風するための空気送風穴が一方の摩砕板に形成さ れている態様がある。 この空気送風穴について、 原料セメントの供給穴 を兼用した場合と、 原料セメン卜の供給穴とは別に一方の摩砕板に形成 した場合とがある。 回転摩砕板を高速で回転した場合、 衝撃による破砕 作用は増大するが、 反面、 遠心力が大きくなるため、 原料セメントの間 隙内での滞留時間が短くなり、 セメン卜粒子同士の擦れ合いによる研摩 作用が減少する。 他方、 回転摩砕板を低速で回転した場合、 衝撃による 破砕作用は減少するが、 反面、 遠心力が小さくなるため、 原料セメント の間隙内での滞留時間が長くなり、 セメン卜粒子同士の擦れ合いによる 研摩作用が増大する。 このように、 研摩作用と破砕作用とのバランスを 考慮しながら回転摩砕板の回転数を設定することになる力 回転摩碎板 を低速で回転させた場合、 原料セメン卜の外周方向の移動量が小さくな り、 排出量 (加工量) 力 s減少することになる。 そこで、 空気送風穴から の送風によって原料セメントを強制的に外周方向に移動させるようにす れば、 この送風量の増減によつて排出量を調節することができる。 又、 突出部について、 これが対向面に張設された網状体である態様、 対向面に突設された多数の突出体である態様、 網状体と突出体の組合せ  There is also a mode in which an air blowing hole for blowing air into the gap is formed in one of the grinding plates. The air blow hole may be used as a supply hole for raw cement, or may be formed on one of the grinding plates separately from the supply hole for raw cement. When the rotary milling plate is rotated at high speed, the crushing action by the impact increases, but on the other hand, the centrifugal force increases, so the residence time in the gap of the raw cement decreases, and the cement particles rub against each other. The polishing action by the sapphire is reduced. On the other hand, when the rotary grinding plate is rotated at a low speed, the crushing action due to the impact is reduced, but the centrifugal force is reduced, so that the residence time of the raw cement in the gap is prolonged and the cement particles rub against each other. The polishing action by the mating increases. Thus, the force that sets the number of rotations of the rotary grinding plate while considering the balance between the grinding action and the crushing action When the rotating grinding plate is rotated at a low speed, the movement of the raw material cement in the outer circumferential direction As a result, the amount of waste (the amount of processing) decreases by s. Therefore, if the raw material cement is forcibly moved in the outer peripheral direction by blowing air from the air blowing hole, the discharge amount can be adjusted by increasing or decreasing the blowing amount. Further, regarding the protruding portion, a mode in which this is a mesh body stretched on the opposing surface, a mode in which it is a number of protruding bodies protruding on the opposing surface, a combination of the net and the protruding body
差替え用紙 (規則 26) である態様がある。 この突出体としては、 突起又は突条、 それに突起と 突条の組合せがある。 Replacement form (Rule 26) There is an embodiment in which The protrusions include protrusions or ridges, and combinations of protrusions and ridges.
又、 突出部について、 突出高さ Hが突出部間の谷部間隔 Lの半分以下 ( H≤2 L ) に形成された突出部分を含んでいる態様がある。 この突出 部は、 原料セメントを間隙内で円周方向へ移動させる作用と、 原料セメ ン卜に衝突させることによる衝撃によって原料セメン卜を破砕させる作 用がある。 し力 しながら、 突出部間の谷部に原料セメント力 '詰まると、 それだけ突出高さが低くなるため、 突出部による作用が低減してしま う。 そこで、 この突出部間の谷部に原料セメントができるだけ詰まらな いようにするために、 この谷部間隔 Lと突出高さ Hとの関係が H≤ 2 Lとなるようにした突出部分を含めることとした。 尚、 H〉2 Lにす ると、 谷部間隔 Lが狭くなり過ぎ、 谷部に原料セメントが詰まりやすく なる。 図面の簡単な説明  Further, there is a mode in which the protruding portion includes a protruding portion formed such that the protruding height H is equal to or less than half (H≤2L) of the valley interval L between the protruding portions. The projecting portion has a function of moving the raw material cement in the gap in the circumferential direction and a function of crushing the raw material cement by an impact caused by collision with the raw material cement. When the raw cement force is clogged in the valleys between the protrusions, the height of the protrusion decreases accordingly, and the effect of the protrusion decreases. Therefore, in order to prevent the raw cement from clogging the valleys between the protruding parts as much as possible, include a protruding part in which the relationship between the valley spacing L and the protruding height H is H≤2L. I decided that. If H> 2L, the valley interval L becomes too narrow, and the valley tends to be clogged with the raw material cement. BRIEF DESCRIPTION OF THE FIGURES
第 1図はこの発明にかかる好ましいセメント摩砕装置の概略断面図で ある。 第 2図はこのセメント摩砕装置に設けられた回転摩砕板の平面 図、 第 3図はこの回転摩碎板に設けられた突出部としての網状体を示す 拡大断面図である。 第 4図及び第 5図はセメント摩砕装置に設けられた 摩砕板の回転駆動形態を示す概略断面図、 第 6図及び第 7図は摩砕板の 対向配置形態を示す概略断面図、 図 8は摩砕板に設けられた供給穴の位 置形態を示す概略断面図、 第 9図〜第 1 1図は摩砕板の間に形成された 間隙の形態を示す概略断面図、 第 1 2図及び第 1 3図は摩砕板に設けら れた空気送風穴の形態を示す概略断面図、 第 1 4図〜第 1 7図は摩砕板 の対向面に設けられた突出部の形態を示す概略平面図、 第 1 8図〜第 2 3図は突出部の断面形状の形態を示すと共に、 突出高さと突出部間の 谷部間隔の関係を示す断面説明図、 第 2 4図及び第 2 5図は突出部の突  FIG. 1 is a schematic sectional view of a preferred cement grinding apparatus according to the present invention. FIG. 2 is a plan view of a rotary grinding plate provided in the cement grinding device, and FIG. 3 is an enlarged cross-sectional view showing a net as a projection provided in the rotary grinding plate. FIGS. 4 and 5 are schematic cross-sectional views showing a rotary driving form of a grinding plate provided in a cement grinding apparatus. FIGS. 6 and 7 are schematic cross-sectional views showing a facing arrangement form of the grinding plates. Fig. 8 is a schematic sectional view showing the position of the supply holes provided in the grinding plate, Figs. 9 to 11 are schematic sectional views showing the form of the gap formed between the grinding plates, and Figs. Figures 13 and 13 are schematic cross-sectional views showing the configuration of the air blow holes provided in the grinding plate, and Figs. 14 to 17 are the shapes of the protrusions provided on the opposing surface of the grinding plate. FIGS. 18 to 23 show cross-sectional shapes of the protruding portions, and are cross-sectional explanatory diagrams showing the relationship between the protruding height and the valley interval between the protruding portions, FIGS. 24 and Fig. 25 shows the protrusion
差替え用紙 (規則 26) 出高さと突出部間の谷部間隔の関係を示す断面説明図である。 発明を実施するための最良の形態 Replacement form (Rule 26) It is sectional explanatory drawing which shows the relationship between protruding height and the space | interval of a valley part between protrusion parts. BEST MODE FOR CARRYING OUT THE INVENTION
以下、 本発明の実施の形態を図面に従って詳述する。  Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings.
第 1図はこの発明にかかる実施の 1形態であるセメント摩砕装置の概 略断面図、 第 2図はこのセメント摩碎装置に設けられた回転摩碎板の平 面図、 第 3図はこの回転摩碎板に設けられた突出部の拡大断面図であ る。 このセメント摩砕装置は、 上下に対向配置した固定摩砕板 1と回転 摩碎板 2とを備え、 この両摩砕板 1, 2の間に間隙 3が形成されてい る。  FIG. 1 is a schematic sectional view of a cement grinding apparatus according to one embodiment of the present invention, FIG. 2 is a plan view of a rotary grinding plate provided in the cement grinding apparatus, and FIG. It is an expanded sectional view of the protrusion provided in this rotary grinding plate. This cement grinding device includes a fixed grinding plate 1 and a rotating grinding plate 2 that are arranged vertically and opposed to each other, and a gap 3 is formed between the grinding plates 1 and 2.
前記固定摩砕板 1は、 金属 (鉄、 铸鉄、 ステンレス等) 、 合成樹脂、 セラミック、 その他の耐摩耗性に優れた材料等で円形に形成され、 その 中心に前記間隙 3に連通する原料セメントの供給穴 1 0力形成されてい る。 尚、 この固定摩砕板 1はケ一シング 4に機枠 4 0を介して固定され ている。 又、 前記ケ一シング 4は、 ステンレスによって円筒状に形成さ れ、 その上端に前記供給穴 1 0に連通する投入ホッパ 4 1力 s形成され、 下端に排出□ 4 2力形成されている。  The fixed grinding plate 1 is made of metal (iron, iron, stainless steel, etc.), synthetic resin, ceramic, other materials having excellent wear resistance, and the like, and is formed in a circular shape. A cement supply hole is formed. The fixed grinding plate 1 is fixed to the casing 4 via a machine frame 40. The casing 4 is formed of stainless steel in a cylindrical shape, and is formed at its upper end with a loading hopper 41 s communicating with the supply hole 10 and at its lower end with a discharge square 42 force.
前記回転摩碎板 2は、 固定摩碎板 1と同様の材質で円形に形成され、 その下面中央部に回転駆動装置 2 0 aが連結されている。 この回転駆動 装置 2 0 aは、 ケーシング 4に軸支された回転軸 2 1が回転摩碎板 2の 下面中央部に連結され、 この回転軸 2 1にプーリ 2 2が取り付けられ、 このプーリ 2 2にベル卜 2 3力3掛け回され、 駆動モータ (図示せず) か らの回転力が回転軸 2 1を介して回転摩碎板 2に伝達される構造となつ ている。 The rotary grinding plate 2 is formed in a circular shape with the same material as the fixed grinding plate 1, and a rotation driving device 20a is connected to a central portion of the lower surface thereof. In this rotary drive device 20a, a rotary shaft 21 pivotally supported by a casing 4 is connected to the center of the lower surface of the rotary grinding plate 2, and a pulley 22 is attached to the rotary shaft 21. The belt 2 is wound around the belt 2 3 times 3 times, and the rotating force from a drive motor (not shown) is transmitted to the rotary grinding plate 2 via the rotating shaft 21.
前記間隙 3は平面状に形成され、 又、 この間隙 3に向けて両摩碎板 1 , 2の外周に沿って突出縁 3 0, 3 0力突設されている。 尚、 この突 出縁 3 0は必ずしも必要でないし、 又、 この突出縁 3 0をいずれカー方  The gap 3 is formed in a planar shape, and protruding edges 30 and 30 are protruded toward the gap 3 along the outer circumferences of the grinding plates 1 and 2. The protruding edge 30 is not always necessary, and the protruding edge 30 is
差替え用紙 (規則 26) の摩砕板に形成する場合もある。 Replacement form (Rule 26) In some cases.
又、 前記両摩砕板 1, 2の対向面 1 1, 2 4には、 それぞれ突出部と しての網状体 5 0, 5 0が張設されている。 回転摩砕板 2の網状体 5 0について説明すると、 第 2図及び第 3図に示すように、 断面円形の 金属線材 5 1が格子状に編まれたもので、 回転摩碎板 2とは別に製作さ れ、 回転摩砕板 2の対向面 2 4に溶接によって取り付けられている。 そ して、 この網状体 5 0は、 これを構成する金属線材 5 1の突出高さ Hが 金属線材 5 1間の谷部間隔 Lの半分以下 (H≤2 L ) に形成された突出 部分を含んでいる。 又、 固定摩砕板 1の網状体 5 0についても同様に形 成されている。 尚、 この網状体 5 0 (突出部) は、 少なくとも回転摩砕 板 2の対向面 2 4に設けられていればよし、。  On the opposing surfaces 11 and 24 of the grinding plates 1 and 2, reticulated bodies 50 and 50 are respectively provided as projections. The mesh 50 of the rotary milling plate 2 will be described. As shown in FIGS. 2 and 3, a metal wire rod 51 having a circular cross section is woven in a lattice shape. It is manufactured separately and attached to the opposing surface 24 of the rotary grinding plate 2 by welding. In addition, this net-like body 50 has a protruding portion formed such that the protruding height H of the metal wire 51 constituting the net is less than half (H≤2 L) of the valley interval L between the metal wires 51. Contains. The mesh 50 of the fixed grinding plate 1 is formed in the same manner. It is sufficient that the mesh body 50 (projection) is provided at least on the facing surface 24 of the rotary grinding plate 2.
この実施の形態にかかるセメント摩砕装置を使用するに際しては、 回 転摩砕板 2を回転駆動装置 2 0 aによって回転させながら、 供給穴 1 0から原料セメントを投入する。 この原料セメントは間隙 3に流入 し、 ここで回転摩砕板 2に設けられた網状体 5 0により連れ回されて円 周方向へ移動すると共に遠心力によって外周方向に移動しながら摩砕さ れる。 即ち、 この移動中に回転摩砕板 2の回転によるセメント粒子同士 の擦れ合いによって研摩されると共に、 網状体 5 0, 5 0に衝突するこ とによる衝撃によって破砕される。 この摩砕加工された原料セメント は、 摩砕セメントとなって間隙 3の外周から排出される。  When using the cement grinding apparatus according to this embodiment, the raw cement is supplied from the supply hole 10 while the rotary grinding plate 2 is rotated by the rotary drive device 20a. This raw material cement flows into the gap 3, where it is swirled by the mesh 50 provided on the rotary milling plate 2, moves in the circumferential direction, and is ground by the centrifugal force while moving in the outer circumferential direction. . That is, during this movement, the cement particles are polished by the rubbing of the cement particles due to the rotation of the rotary grinding plate 2, and are crushed by the impact by colliding with the nets 50, 50. The milled raw cement is discharged from the outer periphery of the gap 3 as milled cement.
このように、 供給穴 1 0から投入された原料セメントが間隙 3に流入 し、 ここで摩砕加工されたのち間隙 3の外周から排出されるため、 原料 セメントを連続して投入すれば、 摩碎加工された摩砕セメン卜を連続し て製造することができる。  As described above, the raw material cement supplied from the supply hole 10 flows into the gap 3, is ground there, and then discharged from the outer periphery of the gap 3. Milled cement can be produced continuously.
又、 この実施の形態では、 両摩砕板 1, 2の外周に沿って突出縁 3 0, 3 0力突設されているため、 セメントの出口が狭くなつている。 これによりセメン卜の排出量が抑制されるため、 原料セメン卜が間隙  Further, in this embodiment, since the protruding edges 30, 30 are protruded along the outer peripheries of the both grinding plates 1, 2, the outlet of the cement is narrow. As a result, the amount of cement discharged is suppressed, so that the raw material cement
差替え用紙 (規則 26) 3を密な状態で移動することになるし、 間隙 3に滞留する時間が長くな る。 従って、 セメント粒子同士の擦れ合いが厚くなると共に、 擦れ合い の時間が長くなり、 この結果、 原料セメントを効率的かつ効果的に摩砕 加工することができる。 Replacement form (Rule 26) 3 will move in a dense state, and the residence time in the gap 3 will increase. Therefore, the friction between the cement particles is increased, and the time for the friction is prolonged. As a result, the raw material cement can be efficiently and effectively ground.
又、 回転摩砕板 2の網状体 5 0は、 原料セメントを間隙 3内で円周方 向へ移動させる作用があり、 又、 両摩砕板 1, 2の網状体 5 0, 5 0は、 原料セメントに衝突させることによる衝撃によつて原料セメン 卜を破砕させる作用があるが、 金属線材 5 1, 5 1間の谷部に原料セメ ントカ詰まると、 それだけ突出高さ力低くなるため、 網状体 5 0による 作用が低減してしまう。 そこで、 この金属線材 5 1 , 5 1間の谷部に原 料セメン卜ができるだけ詰まらないようにするために、 その谷部間隔 Lと突出高さ Hとの関係が H≤ 2 Lとなるようにした突出部分を含める こととした。  Further, the mesh 50 of the rotary milling plate 2 has a function of moving the raw material cement in the circumferential direction in the gap 3, and the meshes 50, 50 of the milling plates 1, 2 However, the impact of the collision with the raw material cement has the effect of crushing the raw material cement. However, if the raw material cement is clogged in the valley between the metal wires 51 and 51, the protruding height becomes lower. The effect of the network 50 is reduced. Therefore, in order to prevent the raw material cement from clogging the valley between the metal wires 51 and 51 as much as possible, the relationship between the valley interval L and the protrusion height H should be H≤2L. We decided to include the protruding part of
尚、 本出願人において、 このセメント摩砕装置を用いて流動性セメン トを製造したときの試験結果の一例を以下に示す。  In addition, the present applicant shows an example of a test result when a fluid cement is manufactured using this cement grinding device.
原料セメン卜として普通ポルトランドセメントを用い、 固定摩碎板 1と回転摩碎板 2の直径を 8 0 c mとし、 回転摩碎板 2を 3 0 0 O r p mで回転させて摩砕セメントを製造した。  Ordinary Portland cement was used as the raw material cement, and the diameter of fixed milling plate 1 and rotating milling plate 2 was set to 80 cm, and rotating milling plate 2 was rotated at 300 O rpm to produce milled cement. .
加工前の原料セメン卜を用いて製造したコンクリー卜と、 加工後の摩 砕セメントを用いて製造したコンクリートのスランブ値を測定したとこ ろ、 原料セメン卜を用いたコンクリートが 1 5 . 5 c mであるのに対 し、 摩砕セメントを用いたコンクリートは 1 8 . 5 c mであった。 又、 原料セメン卜を 8 0 0 °Cに加熱して摩碎セメン卜を製造した場合のスラ ンプ値は 2 0 c mであった。 尚、 1 5 (TC未満では摩砕加工の促進が得 られず、 また、 1 4 0 0 °Cを越えると原料セメントが溶けてしまうた め、 原料セメン卜の加熱の範囲を 1 5 0 °C~ 1 4 0 0 °Cとしている。 この試験結果で明らかなように、 原料セメン卜を摩砕加工することに  When the slamb values of the concrete produced using the raw cement before processing and the concrete produced using the ground cement after processing were measured, the concrete using the raw cement was 15.5 cm. On the other hand, concrete with milled cement was 18.5 cm. In addition, when the raw cement was heated to 800 ° C. to produce a milled cement, the slump value was 20 cm. If the temperature is less than 15 (TC, the grinding process cannot be accelerated, and if the temperature exceeds 140 ° C, the raw material cement will be melted. C ~ 140 ° C. As is evident from the test results, it is necessary to grind the raw material cement.
差替え用紙 (規則 26) よつて流動性を向上することができるし、 原料セメン卜を加熱すれば、 摩砕がより促進され、 効率のよい加工ができる。 Replacement form (Rule 26) Thus, fluidity can be improved, and if the raw material cement is heated, grinding is further promoted and efficient processing can be performed.
以下、 本発明のその他の実施の形態について説明する。 尚、 以下の各 実施の形態において、 前記した第 1図の形態と同一構成部分は図面の符 号を同一にしてその説明を省略する。  Hereinafter, other embodiments of the present invention will be described. In the following embodiments, the same components as those in the embodiment shown in FIG. 1 have the same reference numerals in the drawings, and a description thereof will be omitted.
まず、 摩砕板の回転駆動形態について説明する。  First, a description will be given of a rotation driving mode of the grinding plate.
第 4図は回転摩砕板 2を上側に配置し、 固定摩砕板 1を下側に配置し て対向させた場合を示したもので、 上側の回転摩砕板 2の上面中央部に 回転駆動装置 2◦ bが連結されている。 この回転駆動装置 2 0 bは、 ケーシングに軸支された筒状回転軸 2 5が回転摩砕板 2の上面中央部に 連結され、 この筒状回転軸 2 5にプーリ 2 6力 s取り付けられ、 このプ一 リ 2 6にベルト 2 7力 トけ回され、 駆動モータ (図示せず) 力らの回転 力が筒状回転軸 2 5を介して回転摩砕板 2に伝達される構造となってい る。 そして、 回転摩砕板 2の中心に筒状回転軸 2 5の内部に連通する供 給穴 2 8が形成され、 原料セメン卜が筒状回転軸 2 5の内部を通って供 給穴 2 8から間隙 3に供給される構造となっている。  Fig. 4 shows the case where the rotating grinding plate 2 is placed on the upper side and the fixed grinding plate 1 is placed on the lower side and opposed to each other. Drive 2 ◦ b is connected. In this rotary drive device 20b, a cylindrical rotary shaft 25 supported by a casing is connected to the center of the upper surface of the rotary grinding plate 2, and a pulley 26 force is attached to the cylindrical rotary shaft 25. The belt 27 is rotated by the pulley 26, and the rotational force of a drive motor (not shown) is transmitted to the rotary grinding plate 2 via the cylindrical rotary shaft 25. It has become. A supply hole 28 communicating with the inside of the cylindrical rotary shaft 25 is formed at the center of the rotary milling plate 2, and the raw material cement passes through the inside of the cylindrical rotary shaft 25 and is supplied with the supply hole 28. From the gap 3 to the gap 3.
又、 第 5図は回転方向が逆になるように回転駆動装置 2 0 a , 2 0 bに連結された回転摩砕板 2, 2同士を間隙 3を保持して対向配置 した場合を示したもので、 前記間隙 3に連通する原料セメン卜の供給穴 2 8が上側の回転摩砕板 2に形成されている。 この場合、 突出部は、 両 回転摩砕板 2 , 2にそれぞれ設けてもよいし、 又、 少なくとも一方の回 転摩砕板 2に設けていればよい。  Fig. 5 shows a case where the rotary grinding plates 2, 2 connected to the rotary drive units 20a, 20b are opposed to each other while maintaining a gap 3 so that the rotation direction is reversed. A supply hole 28 for the raw material cement communicating with the gap 3 is formed in the upper rotary milling plate 2. In this case, the protruding portion may be provided on each of the rotary grinding plates 2, 2, or may be provided on at least one of the rotary grinding plates 2.
次に、 摩砕板の向きについて説明する。 なお、 以下の各実施の形態に ついては、 固定摩碎板 1と回転摩碎板 2とを対向配置した場合を示して いる力 第 5図で示したような回転摩砕板 2, 2同士を対向配置した場 合にも適用できる。 又、 以下の各実施の形態を組み合わせてセメント摩 碎装置を構成してもよい。  Next, the direction of the grinding plate will be described. In each of the following embodiments, a force indicating a case where the fixed milling plate 1 and the rotary milling plate 2 are arranged opposite to each other is used to connect the rotary milling plates 2 and 2 as shown in FIG. It can also be applied to the case of facing. Further, a cement grinding apparatus may be configured by combining the following embodiments.
差替え用紙 (規則 26) 第 6図は両摩砕板 1 , 2を左右方向に対向配置した場合を示し、 又、 第 7図は両摩砕板 1, 2を斜め方向に対向配置した場合を示したもので ある。 Replacement form (Rule 26) Fig. 6 shows a case where both grinding plates 1 and 2 are arranged to face each other in the left and right direction, and Fig. 7 shows a case where both grinding plates 1 and 2 are arranged to face each other diagonally.
又、 原料セメントの供給穴 1 0の位置については、 第 8図に示すよう に、 摩碎板 1の中心から偏心した位置に形成してもよい。  Further, the position of the feed hole 10 for the raw cement may be formed at a position eccentric from the center of the milling plate 1 as shown in FIG.
次に、 両摩碎板 1 , 2の間に形成された間隙 3について説明する。 第 9図は間隙 3を上向き円錐状に形成した場合を示し、 又、 第 1 0図 は間隙 3を上向き球面状に形成した場合を示したものである。 尚、 間隙 3を下向き円錐状又は下向き球面状に形成してもよい。  Next, the gap 3 formed between the two grinding plates 1 and 2 will be described. FIG. 9 shows a case where the gap 3 is formed in an upward conical shape, and FIG. 10 shows a case where the gap 3 is formed in an upward spherical shape. The gap 3 may be formed in a downward conical shape or a downward spherical shape.
又、 第 1 1図は間隙 3を中央部から外周部に向けて次第に狭幅に形成 した場合を示したもので、 固定摩砕板 1の対向面 1 1を平坦面に形成 し、 回転摩砕板 2の対向面 2 4を外周部から中央部に向けて次第に深く 窪むような傾斜面に形成している。 尚、 これとは逆に、 固定摩碎板 1の 対向面 1 1を傾斜面に形成し、 回転摩砕板 2の対向面 2 4を平坦面に形 成してもよいし、 固定摩碎板 1及び回転摩砕板 2の対向面 1 1, 2 4を それぞれ傾斜面に形成してもよい。  Fig. 11 shows the case where the gap 3 is gradually narrowed from the center to the outer periphery.The opposing surface 11 of the fixed grinding plate 1 is formed as a flat surface, and the rotary grinding is performed. The opposing surface 24 of the crushing plate 2 is formed as an inclined surface that gradually becomes deeper from the outer periphery toward the center. Contrary to this, the opposed surface 11 of the fixed grinding plate 1 may be formed as an inclined surface, and the opposed surface 24 of the rotary grinding plate 2 may be formed as a flat surface. The opposing surfaces 11 and 24 of the plate 1 and the rotary milling plate 2 may be formed on inclined surfaces, respectively.
次に、 摩砕板に空気送風穴を形成した場合について説明する。  Next, the case where an air blowing hole is formed in the grinding plate will be described.
第 1 2図は上側の固定摩砕板 1に形成された供給穴 1 0を空気送風穴 6〇に兼用した場合を示し、 又、 第 1 3図は上側の回転摩碎板 2に形成 された原料セメン卜の供給穴 2 8とは別に下側の固定摩砕板 1に空気送 風穴 6 1を形成した場合を示している。 この第 1 3図の場合、 空気送風 穴 6 1は、 その吹き出し口が多数の小穴 6 2によって形成され、 この小 穴 6 2は中央部から外周部に向けて斜め方向に開口されている。 尚、 図 中 6 3は空気導入筒である。 前記した空気送風穴 6 0, 6 1の作用につ いては、 前記発明の開示の項で説明したので省略する。  Fig. 12 shows the case where the supply hole 10 formed in the upper fixed grinding plate 1 is also used as the air blowing hole 6〇, and Fig. 13 shows the case where the upper rotating grinding plate 2 is formed. This shows a case where an air blow hole 61 is formed in the lower fixed grinding plate 1 separately from the feed hole 28 for the raw material cement. In the case of FIG. 13, the air blowing hole 61 has its outlet formed by a large number of small holes 62, and the small holes 62 are opened obliquely from the center toward the outer periphery. In the figure, reference numeral 63 denotes an air introducing cylinder. The operation of the air blowing holes 60 and 61 described above has been described in the section of the disclosure of the present invention, and will not be described.
次に、 突出部について第 1 4図〜第 2 5図により説明する。  Next, the protrusion will be described with reference to FIGS. 14 to 25. FIG.
第 1 4図は突出部を対向面 2 4に突設した多数の突出体である多数の  Fig. 14 shows a number of protrusions with protrusions projecting from the facing surface 24.
差替え用紙 (規則 26) 突起 5 2によって形成した場合を示している。 この突起 5 2の平面形状 は、 円形、 角形、 十字形等、 任意に決定できる。 Replacement form (Rule 26) The case where the projection 52 is formed is shown. The planar shape of the projection 52 can be arbitrarily determined, such as a circle, a square, or a cross.
第 1 5図は突出部を対向面 2 4に放射状に突設した多数の突出体であ る多数の突条 5 3によつて形成した場合を示している。 この突条 5 3の 平面形状は、 回転摩碎板 2の回転方向 (矢印方向) に向いた面が凹状に なるようにした円弧形状に形成されている。 尚、 この突条 5 3の平面形 状は、 このほ力 >、 直線形状、 波形状等、 網形状、 蜘蛛の巣形状等、 任意 に決定できる。  FIG. 15 shows a case where the projecting portion is formed by a large number of projecting ridges 53 which are a large number of projecting bodies projecting radially from the facing surface 24. The planar shape of the ridge 53 is formed in an arc shape in which the surface of the rotary grinding plate 2 in the rotation direction (the direction of the arrow) is concave. The plane shape of the ridge 53 can be arbitrarily determined, such as a force, a linear shape, a wavy shape, a net shape, a spider web shape, or the like.
又、 第 1 6図は突出部を対向面 2 4に突設した多数の突起 5 2と蜘蛛 の巣形状に形成した多数の突条 5 3との組合せによって形成した場合を 示している。  FIG. 16 shows a case where the projections are formed by a combination of a number of projections 52 projecting from the facing surface 24 and a number of projections 53 formed in a spider web shape.
又、 第 1 7図は突出部を網状体 5 0と突起 5 2と突条 5 3の組合せに よって形成した場合を示している。  FIG. 17 shows a case where the protruding portion is formed by a combination of the net 50, the protrusion 52, and the protrusion 53.
又、 突出部 5の断面形状については、 第 1 8図のように四角形断面、 第 1 9図のように三角形断面、 第 2 0図のように円形断面、 第 2 1図の ように台形断面等に形成できるほか、 これ以外に、 例えば、 半円形等に 形成してもよい。  Regarding the cross-sectional shape of the protruding portion 5, a rectangular cross-section as shown in Fig. 18, a triangular cross-section as shown in Fig. 19, a circular cross-section as shown in Fig. 20, and a trapezoidal cross-section as shown in Fig. 21 In addition, it may be formed in a semicircle or the like.
又、 突出部 5の断面形状について、 例えば、 第 2 2図のように断面形 状は同一の円形断面として、 その大きさを異ならせたり、 又、 第 2 3図 のように四角形断面と三角形断面を組合せるというように、 異なる断面 形状のものを組み合わせてもよい。  Regarding the cross-sectional shape of the protruding portion 5, for example, as shown in FIG. 22, the cross-sectional shape may be the same circular cross-section, and the size may be different. Alternatively, as shown in FIG. Different cross-sectional shapes may be combined, such as combining cross-sections.
又、 突出部 5の突出高さ Hと谷部間隔 Lの関係について、 第 1 8図及 び第 2 1図のように突出部を四角形断面や台形断面とした場合は、 谷部 間隔 Lは、 突出部 5の上端縁 5 4からの距離をいい、 又、 第 1 9図及び 第 2 0図のように突出部を三角形断面や円形断面にした場合は、 突出部 5の頂 、 5 5からの距離をいう。 又、 第 2 2図及び第 2 3図のように、 突出高さ力 s異なる場合には、 谷部間隔 Lとの関係式 (H≤2 L ) でいう Regarding the relationship between the protruding height H of the protruding portion 5 and the valley interval L, when the protruding portion has a rectangular cross section or a trapezoidal cross section as shown in FIGS. 18 and 21, the valley interval L is The distance from the upper edge 54 of the protruding portion 5. When the protruding portion has a triangular cross section or a circular cross section as shown in FIGS. 19 and 20, the top of the protruding portion 5 The distance from Also, as shown in Fig. 22 and Fig. 23, when the protruding height force s is different, it is expressed by the relational expression with the valley interval L (H≤2L)
差替え用紙 (規貝 IJ26) 突出高さ Hは、 高さが低い方の突出部 5 aの突出高さをいう。 尚、 前記 した突出部を網状体 5 0で形成した場合について、 金属線材 5 1の交差 部については、 金属線材 5 1同士の重なりによって突出高さが金属線材 5 ]の 2倍になるため、 この交差部と交差部以外の部分では突出高さが 異なることになる。 この場合にも、 突出高さ Hは、 高さが低い方の突出 部の高さをいう。 Replacement paper (Kaikai IJ26) The protrusion height H refers to the protrusion height of the lower protrusion 5a. In the case where the protruding portion is formed of the mesh body 50, at the intersection of the metal wires 51, the protruding height is twice as large as that of the metal wire 5] due to the overlap of the metal wires 51. The protruding height is different between the intersection and the portion other than the intersection. Also in this case, the protrusion height H refers to the height of the protrusion having the lower height.
尚、 参考までに、 突出高さ Hと谷部間隔 Lの関係で、 H〉2 Lとした 場合の例を第 2 4図及び第 2 5図に示す。 この例では、 谷部が狭くな り、 ここ力 '原料セメン卜によって目詰まりを起こしやすくなるという不 具合が生じる。  For reference, FIGS. 24 and 25 show examples of the case where H> 2 L in the relationship between the protrusion height H and the valley interval L. In this example, the valley becomes narrower, which causes a problem that the raw material cement tends to cause clogging.
又、 突出部について、 突出高さ Hと谷部間隔 Lとの関係が H≤2しと なる突出部分は、 突出部全体の 2 0 %以上を含んでいることが望まし レ、。 好ましい形態としては、 突出部全体の 8 0 %lil±を含むように形成 した場合となる力 少なくとも突出部全体の 2 0 %以上を含んでいれ ば、 摩砕効率は低下するものの、 ある程度の摩砕効果が得られる。  In addition, it is desirable that the protruding portion in which the relationship between the protruding height H and the valley interval L satisfies H≤2 includes 20% or more of the entire protruding portion. In a preferred form, the force formed when including 80% lil ± of the entire protruding portion is at least 20% or more of the entire protruding portion. A crushing effect is obtained.
2 0 %未満では摩碎効率カ^く過ぎ、 実用化には不適といえる。 このほか、 摩砕板の材質、 摩砕板の直径、 回転速度、 間隙のクリアラ ンス等は、 摩砕の度合や処理量等に応じて適宜に決定する。 又、 回転駆 動装置についても、 駆動源からの回転力をベルト、 チェン、 歯車等の伝 達手段で摩砕板に伝達することができる構造であればよい。 産業上の利用可能性  If it is less than 20%, the grinding efficiency is too high and it can be said that it is not suitable for practical use. In addition, the material of the attrition plate, the diameter of the attrition plate, the rotation speed, the clearance of the gap, and the like are appropriately determined according to the degree of attrition, the throughput, and the like. Also, the rotary drive device may have any structure as long as the rotary force from the drive source can be transmitted to the grinding plate by a transmission means such as a belt, a chain, and a gear. Industrial applicability
以上のように、 本発明にかかるセメント摩砕装置にあっては、 これで 加工した摩砕セメントを、 建築産業におけるコンクリート建築物、 土木 産業におけるコンクリ一卜構造物、 その他コンクリ一卜製品の原料とし て使用できる。 特に、 このセメント摩碎装置によって加工された摩砕セ メントを用いると、 流動性か く、 コンクリートのヮ一力ピリティーが  As described above, in the cement grinding apparatus according to the present invention, the ground cement thus processed is used as a raw material for concrete buildings in the construction industry, concrete structures in the civil engineering industry, and other concrete products. Can be used as In particular, the use of the milled cement processed by this cement milling equipment makes it possible to reduce the fluidity of concrete and to increase the power of concrete.
差替え用紙 (規則 26) 向上すると共に、 高密度できめが細かく、 高耐久性のコンクリー卜が得 られることから、 施工が簡単で、 仕上がりが良い高品質のコンクリート を製造でき、 各種のコンクリー卜産業に有用に使用することができる。 又、 このセメント摩砕装置による加工工程は、 常法のセメント製造ェ 程に組み込むことができること力 ら、 セメン卜製造ブラン卜に有用に使 用することができる。 Replacement form (Rule 26) It can be used for various concrete industries because it can produce high-quality concrete that is easy to apply and has a good finish because it can improve the density and provide high-density, fine-grained and highly durable concrete. Can be. In addition, the processing step using this cement grinding device can be usefully used for a cement production brand because it can be incorporated into a conventional cement production process.
差替え用紙 (規則 26) Replacement form (Rule 26)

Claims

請求の範囲 The scope of the claims
1 . 回転駆動装置に連結された回転摩砕板と機枠に固定された固定摩 碎板とが間隙を保持して回転摩碎板の軸方向に対向配置され、 前記間隙 に連通する原料セメントの供給穴力一方の摩砕板に形成され、 少なくと も回転摩砕板の対向面に突出部力5設けられていることを特徴としたセメ ント摩砕装置。 1. A rotating cement plate connected to a rotary drive and a fixed grinding plate fixed to the machine frame are arranged opposite to each other in the axial direction of the rotating grinding plate with a gap therebetween, and the raw material cement communicates with the gap. A cement grinding device characterized in that a supply hole force is formed on one of the grinding plates, and at least a protruding portion force 5 is provided on a facing surface of the rotating grinding plate.
2 - 回転方向が逆になるように回転駆動装置に連結された回転摩碎板 同士力撊隙を保持して回転摩砕板の軸方向に対向配置され、 前記間隙に 連通する原料セメン卜の供給穴力—方の摩砕板に形成され、 少なくとも —方の回転摩砕板の対向面に突出部力設けられていることを特徴とした セメント摩枠装置。  2-The rotating milling plates connected to the rotary driving device so that the rotating directions are opposite to each other, and are arranged opposite to each other in the axial direction of the rotary milling plate while maintaining a force gap therebetween, and the raw material cement communicating with the gap is formed. A cement grinding frame device formed on a grinding plate having a supply hole force, and a projection force provided on at least an opposing surface of the rotating grinding plate having a surface.
3 - 請求の範囲第 1項又は第 2項記載のセメント摩砕装置において、 両摩砕板力 U:下方向に対向配置されているセメント摩砕装置。  3-The cement grinding device according to claim 1 or 2, wherein the both grinding plate forces U: the cement grinding device arranged to face downward.
. 請求の範囲第 1項又は第 2項記載のセメン卜摩砕装置において、 両摩砕板力左右方向に対向 S置されているセメント摩碎装置。  3. The cement grinding apparatus according to claim 1 or 2, wherein both grinding plate forces are opposed to each other in the left-right direction.
5 , 請求の範囲第 1項又は第 2項記載のセメン卜摩砕装置において、 両摩碎板力 4め方向に対向配置されているセメン卜摩砕装置。  5. The cement grinding apparatus according to claim 1 or 2, wherein the both grinding plate forces are opposed to each other in the fourth direction.
6 . 請求の範囲第 1項又は第 2項記載のセメント摩碎装置において、 原料セメン卜の供給穴力 s摩砕板の中心に形成されているセメント摩 置。  6. The cement grinding apparatus according to claim 1 or 2, wherein a supply force of a raw material cement is provided at a center of the grinding plate.
7 . 請求の範囲第 1項又は第 2項記載のセメント摩碎装置において、 原料セメン卜の供給穴が摩砕板の中心から偏心した位置に形成されてい るセメント摩砕装置。  7. The cement grinding apparatus according to claim 1, wherein the supply hole for the raw material cement is formed at a position eccentric from the center of the grinding plate.
8. 請求の範囲第 1項又は第 2項記載のセメント縻砕装置において、 間隙が平面状に形成されているセメン卜摩砕装置。  8. The cement grinder according to claim 1 or 2, wherein the gap is formed in a plane.
9 - 請求の範囲第 1 ¾Χは第 2項記載のセメント摩砕装 Sにおいて、 間隙が円錐状に形成されているセメント摩砕装置。 9-Claim 1¾Χ is the cement grinding equipment S described in paragraph 2, A cement grinding device with a conical gap.
1 0 . 請求の範囲第 1項又は第 2項記載のセメント摩砕装置におい て、 間隙カ 面状に形成されているセメント摩碎装置。  10. The cement grinding device according to claim 1 or 2, wherein the cement grinding device is formed in a gap-like surface.
1 1 . 請求の範囲第 1頊又は第 2項記載のセメント縻砕装置におい て、 PB1]隙が中央部から外周部に向けて次第に狭幅に形成されているセメ ン卜摩砕装置。 11. The cement grinder according to claim 1 or 2, wherein the PB 1 ] gap is gradually narrowed from the center to the outer periphery.
1 2 . 請求の範囲第 1項又は第 2項記載のセメント摩砕装置におい て、 少なくとも一方の摩砕板の外周に沿って突出縁が間隙に向けて突設 されているセメン卜摩碎装置。  12. The cement grinding device according to claim 1 or 2, wherein a protruding edge projects toward a gap along an outer periphery of at least one of the grinding plates. .
1 3 . 請求の範囲第 1項又は第 2項記載のセメント摩砕装置におい て、 間隙に空気を送風するための空気送風穴が一方の摩砕板に形成され ているセメント縻砕装 s。  13. The cement chrysler according to claim 1 or 2, wherein an air blowing hole for blowing air into the gap is formed in one of the grinding plates.
1 4 . 請求の範囲第 1 3項記載のセメン卜摩砕装置において、 空気送 風穴が原料セメン卜の供給穴を兼用しているセメント摩碎装置。  14. The cement grinding apparatus according to claim 13, wherein the air blowing hole also serves as a supply hole for the raw material cement.
1 5 . 請求の範囲第 1 3項記載のセメン卜摩砕装置において、 空気送 風穴が原料セメン卜の供給穴とは別に一方の摩砕板に形成されているセ メント摩 置。  15. The cement grinding apparatus according to claim 13, wherein the air blowing hole is formed in one of the grinding plates separately from the supply hole for the raw material cement.
1 6 . 請求の範囲第 1項又は第 2項記載のセメン卜摩砕装置におい て、 突出部力《対向面に張設された網状体であるセメント摩砕装置。 16. The cement grinding apparatus according to claim 1 or 2, wherein a force of the projecting portion is << a mesh body stretched on the facing surface.
1 7 . 請求の範囲第 1項又は第 2項記載のセメント摩砕装置におい て、 突出部が対向面に突設された多数の突出体であるセメント摩砕装 置。 17. The cement grinding apparatus according to claim 1 or 2, wherein the projections are a number of protrusions projecting from the opposing surface.
1 8 . 請求の範囲第 1項又は第 2項記載のセメント摩砕装置におい て、 突出部が対向面に張設された網状体と、 対向面に突設された突出体 の組合せであるセメン卜摩砕装置。  18. The cement grinding apparatus according to claim 1 or 2, wherein the cement is a combination of a net-like body having a protruding portion stretched on the facing surface and a protruding body projecting from the facing surface. Trimming device.
1 9 . 請求の範囲第 1項又は第 2項記載のセメント摩碎装置におい て、 突出部は、 突出高さ Ηが突出部間の谷部間隔 Lの半分以下 (Η≤ 2 L) に形成された突出部分を含んでいるセメント摩砕装置。 19. The cement grinding apparatus according to claim 1 or 2, wherein the projecting portion has a projecting height Η of not more than half of a valley interval L between projecting portions (Η≤ 2 L) Cement milling device including a protruding part formed in it.
20. 請求の範囲第 1項又は第 2項記載のセメン卜摩砕装置におい て、 原料セメント力;比表面積 2000 cm2 ZgJiLhのセメントクリン 力を含んでいるポル卜ランドセメント系であるセメント縻砕装置。20. The cement grinder according to claim 1 or 2, wherein the cement churning is a Portland cement system containing a raw material cement power; a cement clean power of 2000 cm 2 ZgJiLh. apparatus.
21 - 請求の範囲第 1項又は第 2項 R載のセメント摩砕装置におい て、 原料セメン卜が比表面積 2000 cm2 /giiU:のセメントクリン 力を含んでいる混合セメン卜系であるセメント摩砕装置。 21-Claim 1 or 2 In the cement grinding apparatus described in R above, the cement cement is a mixed cement system in which the raw material cement has a specific surface area of 2,000 cm 2 / giiU. Crusher.
22. 請求の範囲第 1項又は第 2項記載のセメン卜摩砕装置におい て、 原料セメン卜が 150 〜 140 crcに加熱されているセメン卜摩 砕装置。  22. The cement grinding apparatus according to claim 1 or 2, wherein the raw material cement is heated to 150 to 140 crc.
PCT/JP1998/002238 1998-05-21 1998-05-21 Cement grinder WO1999059932A1 (en)

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1541257A2 (en) * 2003-12-13 2005-06-15 Jörg Häring Device for regenerating foundry sand
WO2011077422A1 (en) * 2009-12-22 2011-06-30 Innovert Investments A.L. Ltd Method and apparatus for rubber grinding and reclaiming
CN102794390A (en) * 2012-07-23 2012-11-28 机械工业第四设计研究院 Used sand reclamation plant
KR101471937B1 (en) * 2014-04-24 2014-12-11 (유)금강환경 Vibration type polishing device for aggregate
KR101479744B1 (en) * 2013-06-14 2015-01-15 주식회사 리텍 Apparatus for peeling and removing of cement
CN107159380A (en) * 2017-05-25 2017-09-15 北京康普锡威科技有限公司 A kind of vertical powder spheroidization device, spheroidizing of powder method and application
RU2730327C1 (en) * 2016-11-29 2020-08-21 Анхуи Гвг Нью Материал Ко., Лтд Complex production system and method of ecological recovery and recycling of rubber wastes

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6053654B2 (en) * 1978-05-29 1985-11-27 株式会社細川粉体工学研究所 Mill-type grinding device
JPH0532438A (en) * 1991-07-31 1993-02-09 Shimizu Corp Production of spherical cement in high efficiency

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6053654B2 (en) * 1978-05-29 1985-11-27 株式会社細川粉体工学研究所 Mill-type grinding device
JPH0532438A (en) * 1991-07-31 1993-02-09 Shimizu Corp Production of spherical cement in high efficiency

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1541257A2 (en) * 2003-12-13 2005-06-15 Jörg Häring Device for regenerating foundry sand
EP1541257A3 (en) * 2003-12-13 2005-10-05 Jörg Häring Device for regenerating foundry sand
WO2011077422A1 (en) * 2009-12-22 2011-06-30 Innovert Investments A.L. Ltd Method and apparatus for rubber grinding and reclaiming
CN102753323B (en) * 2009-12-22 2014-12-17 格林-加姆橡胶回收有限公司 Method and apparatus for rubber grinding and reclaiming
US8955779B2 (en) 2009-12-22 2015-02-17 Green-Gum Rubber Recycle Ltd. Method and apparatus for rubber grinding and reclaiming
RU2544651C2 (en) * 2009-12-22 2015-03-20 Грин-Гам Раббер Ресайкл Лтд. Method and device for grinding and recovery of rubber
CN102794390A (en) * 2012-07-23 2012-11-28 机械工业第四设计研究院 Used sand reclamation plant
KR101479744B1 (en) * 2013-06-14 2015-01-15 주식회사 리텍 Apparatus for peeling and removing of cement
KR101471937B1 (en) * 2014-04-24 2014-12-11 (유)금강환경 Vibration type polishing device for aggregate
RU2730327C1 (en) * 2016-11-29 2020-08-21 Анхуи Гвг Нью Материал Ко., Лтд Complex production system and method of ecological recovery and recycling of rubber wastes
CN107159380A (en) * 2017-05-25 2017-09-15 北京康普锡威科技有限公司 A kind of vertical powder spheroidization device, spheroidizing of powder method and application

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