JPH0549887A - Static type fluid mixer and its production - Google Patents

Static type fluid mixer and its production

Info

Publication number
JPH0549887A
JPH0549887A JP29099391A JP29099391A JPH0549887A JP H0549887 A JPH0549887 A JP H0549887A JP 29099391 A JP29099391 A JP 29099391A JP 29099391 A JP29099391 A JP 29099391A JP H0549887 A JPH0549887 A JP H0549887A
Authority
JP
Japan
Prior art keywords
mixer
fluid mixer
passage
concrete
mixing
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
Application number
JP29099391A
Other languages
Japanese (ja)
Other versions
JP3107877B2 (en
Inventor
Hisao Kojima
久夫 小嶋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP03290993A priority Critical patent/JP3107877B2/en
Publication of JPH0549887A publication Critical patent/JPH0549887A/en
Application granted granted Critical
Publication of JP3107877B2 publication Critical patent/JP3107877B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PURPOSE:To provide the static type fluid mixer which is high in the efficiency of mixing high-viscosity materials, granular substances, concrete, etc., has excellent wear resistance and corrosion resistance, and is low in cost. CONSTITUTION:This static type fluid mixer 1 has a passage pipe 2 in which fluids FA and FB flow and plural pieces of vane bodies 3, 4 which rotate spirally on the inner peripheral surface of this passage pipe 2. The fluids FA and FB are mixed with high efficiency without generating troubles, such as stagnating and clogging, in the mixer in this way. This mixer can be produced at the low cost from a stage for joining the spiral vane bodies 3, 4 on the inner peripheral surfaces of the passage pipes 2a, 2b longitudinally divided to plural pieces and a stage for joining the divided planes of the passage pipes 2a, 2b to each other.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は混合のための機械的可動
部分を有しないで2種以上の流体を混合する静止型流体
混合器及びその製造方法に関し、更に詳述すれば、混
合、分散、乳化、ガス吸収、希釈及び溶解等の工程にお
いて使用される静止型流体混合器及び製造方法に関す
る。特に、粉粒体、砂利、コンクリート等の固体同士の
混合、及び高粘度物質の混合に、層流域で利用する場合
に最適な静止型流体混合器及び製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a static fluid mixer for mixing two or more kinds of fluids without a mechanical moving part for mixing and a method for producing the same, and more specifically, mixing and dispersion. , A static fluid mixer used in processes such as emulsification, gas absorption, dilution and dissolution, and a manufacturing method. In particular, the present invention relates to a static fluid mixer and a manufacturing method that are optimal when used in a laminar flow region for mixing solids such as powder, gravel, and concrete, and for mixing highly viscous substances.

【0002】[0002]

【従来の技術】この種の静止型流体混合器は、化学工
業、食品工業、公害防止関連工業、電子工業等の多くの
分野で、化学反応装置及び生物反応装置等用の機械的可
動部分を有しない混合器として多数使用されている。而
して、この流体混合器の製造手段としては、右捻り又は
左捻りの螺旋状の羽根をパイプ内に挿入し、隣接する羽
根同士を溶接又はロー付け等の手段により固定するもの
がある(特公昭44−8290号)。また、右捻り又は
左捻りの螺旋状の羽根をパイプ内に挿入し、隣接する羽
根同士を相互に係止させ又は嵌合してパイプ内に配置す
る技術もある(西独公開番号第2262016号)。更
に、右捻り又は左捻りの螺旋状の羽根を隣接する羽根間
に支持具を配置してパイプ内に挿入し、羽根をこの支持
具により固定して連結するものもある(米国特許第3,
953,002号)。更にまた、右又は左に捻じられた
バッフル板を管状ハウジング内に挿入し、前記バッフル
板の両端突出部に形成した凹溝同士を係合させて両者を
連結したものもある(特公平1−31928号)。そし
て、更に、ロストワックス型の鋳型内にプラスチックス
或いは金属を鋳造することによってミキサー要素を製造
し、このミキサー要素をケーシング内に配置したものも
ある(特公昭57−4369号)。
2. Description of the Related Art A static fluid mixer of this type has mechanical moving parts for chemical reaction devices and biological reaction devices in many fields such as chemical industry, food industry, pollution control industry, and electronics industry. Many are used as mixers that do not have. As a manufacturing method of this fluid mixer, there is a method of inserting right-handed or left-handed spiral blades into a pipe and fixing adjacent blades by means such as welding or brazing ( Japanese Patent Publication No. 44-8290). There is also a technique in which a right-handed or left-handed spiral blade is inserted into a pipe, and adjacent blades are locked or fitted to each other and placed in the pipe (West German publication number 2262016). .. Further, there is also one in which a right-handed or left-handed spiral blade is placed between adjacent blades and inserted into a pipe, and the blades are fixed and connected by the support (US Pat.
953,002). Furthermore, there is also one in which a baffle plate twisted to the right or left is inserted into a tubular housing, and concave grooves formed on both end projections of the baffle plate are engaged with each other to connect the two (Patent Publication 1- 31928). Further, there is also one in which a mixer element is manufactured by casting plastics or metal in a lost wax type mold, and the mixer element is arranged in a casing (Japanese Patent Publication No. 57-4369).

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上述し
た従来の静止型流体混合器は、高粘度物質、粉粒体等を
混合させる場合に、必ずしも流体の混合効率が十分なも
のとはいえない欠点がある。特に、コンクリート、砂利
等の混合に利用した場合、混合器内で閉塞を起し、混合
は困難である。更に、前記ミキサー要素(特公昭57−
4369号)による混合器は、流体が通流する流体通路
の有効断面積が小さい為に、高粘度物質、粉粒体の混合
に利用した場合、隣接するミキサー要素とミキサー要素
との接合面で、流体の淀みや滞留が生じて流体通路の閉
塞などのトラブルが発生し易い。又、製造工程も複雑な
工程で行なわれるので、製造コストも高くなる欠点があ
る。更に又、上述した各製造手段は、いずれも製造が容
易でないという欠点がある。特に、羽根同士を溶接又は
ロー付けした場合には、その接合部分で機械的強度が弱
く、ねじれ応力が印加された場合に、溶接部が破損した
り、折損したりする欠点もある。また、大型の場合は製
造コストが高いという問題もある。更に、混合器の耐摩
擦性、耐蝕性を向上させる為に、混合器内面をゴム、プ
ラスチックス、セラミックス等で被覆処理を行なうに
も、製造工程が複雑な為に困難が伴なう。本発明はかか
る問題点に鑑みてなされたものであって、粉粒体、高粘
度物質、コンクリート等の流体混合に適し、且つ耐摩耗
性、耐蝕性に優れ、又ねじれ応力に強い静止型流体混合
器及び容易に且つ低コストで製造できる流体混合器の製
造方法を提供することを目的とする。
However, the conventional static fluid mixer described above does not always have sufficient fluid mixing efficiency when mixing a high-viscosity substance, powder or the like. There is. In particular, when it is used for mixing concrete, gravel, etc., it causes blockage in the mixer and mixing is difficult. Furthermore, the mixer element (Japanese Patent Publication No. 57-
The mixer according to No. 4369) has a small effective cross-sectional area of the fluid passage through which the fluid flows. Therefore, when it is used for mixing a high-viscosity substance and powdery particles, the mixer has a joint surface between adjacent mixer elements. However, stagnation or retention of the fluid easily occurs and troubles such as clogging of the fluid passage are likely to occur. Further, since the manufacturing process is performed in a complicated process, there is a drawback that the manufacturing cost becomes high. Furthermore, each of the above-mentioned manufacturing means has a drawback that manufacturing is not easy. In particular, when the blades are welded or brazed to each other, the mechanical strength of the joint is weak, and there is a drawback that the welded portion is broken or broken when a torsional stress is applied. There is also a problem that the manufacturing cost is high in the case of a large size. Further, even if the inner surface of the mixer is coated with rubber, plastics, ceramics or the like in order to improve the abrasion resistance and the corrosion resistance of the mixer, it is difficult because the manufacturing process is complicated. The present invention has been made in view of the above problems, and is a static fluid suitable for mixing powders, highly viscous substances, fluids such as concrete, and having excellent wear resistance, corrosion resistance, and torsion stress. An object of the present invention is to provide a mixer and a manufacturing method of a fluid mixer which can be manufactured easily and at low cost.

【0004】[0004]

【課題を解決するための手段】本発明に係る静止型流体
混合器は、流体が通流する通路管と、この通路管の内周
面に螺旋状に回転する複数個の羽根体とを有する。ま
た、本発明に係る静止型流体混合器の製造方法は、長手
方向に複数個に分割された通路管の内周面に螺旋状の羽
根体とを接合する工程と、この通路管の分割面同士を接
合する工程とを有していることを特徴とする。
A static fluid mixer according to the present invention has a passage pipe through which a fluid flows, and a plurality of blades spirally rotating on the inner peripheral surface of the passage pipe. .. Further, a method of manufacturing a static fluid mixer according to the present invention comprises a step of joining a spiral blade body to an inner peripheral surface of a passage tube divided into a plurality of pieces in a longitudinal direction, and a division surface of the passage tube. And a step of joining them to each other.

【0005】[0005]

【作用】本発明は、図1に示すように、混合器1は、通
路管2の内周面に、複数個の螺旋状の羽根体3及び4が
接合されている。羽根体3は右捻り(時計方向)に90
°捻じられている。羽根体4は左捻り(反時計方向)に
90°捻じられている。また、図2及び図3に示すよう
に、混合器1内の中心部は一定の幅で長手方向に開口部
6、7を有している。更に、羽根体3及び羽根体4との
間に一定の間隔でスペース部5を有している。更にま
た、羽根体3と羽根体4の端縁とはスペース部5を介し
て直交して交互に配置されている。なお、開口部6、7
は長手方向に於いて、直線でも、曲線でもよい。又、開
口断面積が異なるテーパー状でもよい。同一捻り方向の
羽根体3及び4の個数は2枚のみでなく、1枚又は2枚
以上でもよい。更に、羽根体3と羽根体4との間にスペ
ース部5を設けずに、羽根体3と羽根体4とを連続的に
隣接して交互に配置して混合器1を構成してもよい。な
お、羽根体3、4の捻り角度は90゜のみでなくて任意
に設定できる。本発明は、混合器1内に2種以上の流体
FAとFBを流入すると、一部の流体は通路管2内に接
合されている羽根体3に沿って時計方向に回転しながら
通流し、スペース部5で合流し、また、他の一部の流体
は羽根体3の開口部7の長手方向において、せん断作用
を受ける。更に、合流した流体FAとFBは羽根体4の
上流側の端縁で分割されて一部の流体は羽根体4に沿っ
て反時計方向に回転しながら通流し、且つ同様に羽根体
4の開口部7でせん断作用を受ける。このように、2種
以上の流体FAとFBは混合器1内で、分割、合流、転
位、せん断作用を繰返しながら、付着、滞留、閉塞など
のトラブルを発生することなく高効率で撹拌混合され
る。更に、本発明の製造方法においては、先ず、分割さ
れた半同筒状の通路管2a、2bの内周面の所定の位置
に、螺旋状の羽根体3、4を接着、溶接等の手段により
接合し、次に、半同筒状の通路管2a、2b同士を分割
面8で溶接等の手段により接合する。この場合、分割面
8同士を溶接せずに、開閉自在になるように締め付け具
等の手段を用いて接合、固定してもよい。なお、羽根体
3、4は鍛造、鋳造、射出成型などの手段により容易に
製造される。このようにして、極めて容易に高性能の静
止型流体混合器1を製造することができる。更に、混合
器内面に、ゴム、プラスチックス、セラミックス等によ
り被覆処理を行なう場合、半同筒状の通路管2a、2b
の内面及び接合された羽根体3、4表面に、塗布、溶
射、蒸着などの手段により容易に被覆処理ができる。こ
のようにして耐摩耗性、耐蝕性に優れた静止型流体混合
器を低コストで容易に製造できる。
According to the present invention, as shown in FIG. 1, in the mixer 1, a plurality of spiral blades 3 and 4 are joined to the inner peripheral surface of the passage tube 2. The blade 3 is twisted to the right (clockwise) by 90
° twisted. The blade body 4 is twisted leftward (counterclockwise) by 90 °. Further, as shown in FIGS. 2 and 3, the central portion of the mixer 1 has openings 6 and 7 with a constant width in the longitudinal direction. Further, space portions 5 are provided at a constant interval between the blade body 3 and the blade body 4. Furthermore, the blade body 3 and the edge of the blade body 4 are arranged alternately at right angles to each other with the space portion 5 interposed therebetween. The openings 6 and 7
May be straight or curved in the longitudinal direction. Further, it may be tapered with different opening cross-sectional areas. The number of blades 3 and 4 in the same twisting direction is not limited to two, and may be one or two or more. Further, the mixer 1 may be configured by arranging the blade bodies 3 and the blade bodies 4 continuously adjacent to each other and alternately without providing the space portion 5 between the blade bodies 3 and 4. .. The twisting angles of the blades 3 and 4 are not limited to 90 ° and can be set arbitrarily. According to the present invention, when two or more kinds of fluids FA and FB flow into the mixer 1, some of the fluids flow while rotating clockwise along the blade body 3 joined in the passage tube 2, The fluid merges in the space portion 5, and a part of the other fluid undergoes a shearing action in the longitudinal direction of the opening 7 of the blade body 3. Further, the merged fluids FA and FB are divided at the upstream edge of the blade body 4 so that a part of the fluid flows while rotating counterclockwise along the blade body 4, and likewise, of the blade body 4. The opening 7 receives a shearing action. As described above, the two or more kinds of fluids FA and FB are stirred and mixed in the mixer 1 with high efficiency without causing troubles such as adhesion, retention and blockage while repeating division, merging, dislocation and shearing action. It Further, in the manufacturing method of the present invention, first, the spiral blades 3, 4 are bonded or welded to a predetermined position on the inner peripheral surfaces of the divided semi-cylindrical passage tubes 2a, 2b. Then, the semi-same tubular passage tubes 2a and 2b are joined to each other at the dividing surface 8 by welding or the like. In this case, the divided surfaces 8 may be joined and fixed by means such as a fastening tool so that they can be opened and closed without being welded to each other. The blades 3 and 4 are easily manufactured by means of forging, casting, injection molding or the like. In this way, the high performance static fluid mixer 1 can be manufactured very easily. Further, when the inner surface of the mixer is coated with rubber, plastics, ceramics or the like, the semi-cylindrical passage pipes 2a, 2b are provided.
The inner surface and the surfaces of the joined blades 3 and 4 can be easily covered by a means such as coating, thermal spraying or vapor deposition. In this way, a static fluid mixer having excellent wear resistance and corrosion resistance can be easily manufactured at low cost.

【0006】[0006]

【実施例】次に、本発明による静止型流体混合器の実施
例について更に具体的に説明する。図4は、本発明の静
止型流体混合器を利用して、コンクリートと急結剤との
混合に応用した場合の概略の系統図である。セメント、
砂利、水等から構成されるコンクリートはコンクリート
ポンプ9を介してコンクリート供給ライン10を通じて
静止型流体混合器14内に一定量圧送される。一方、短
時間でコンクリートを固化させる急結剤は、急結剤タン
ク11から急結剤ポンプ12を介して、急結剤供給ライ
ン13を通じて混合器14内に一定量圧送される。圧送
されたコンクリート及び急結剤は混合器14内で、開口
部を有する螺旋状の右及び左捻りの羽根体3、4によ
り、分割、合流、転位、せん断作用を繰返しながら連続
的に撹拌混合されて、均質なコンクリートと急結剤との
混合組成物が製造できる。このように、コンクリートと
急結剤との混合に適用した場合、混合器14内の羽根体
3、4は単純な形状であるので流動抵抗も小さく、ま
た、淀み部がないのでコンクリートの滞留、閉塞などに
よるトラブルの発生がなく、且つ、高効率で混合でき
る。更に、この製造方法によると、使用直前に必要量だ
け混合できるので、原材料の損失が少なくなる。又、こ
の混合組成物を吹付けに利用した場合、吹付け後、すぐ
に硬化する。従って、吹付けられたコンクリート層を厚
く施工でき、又、吹付け面からのコンクリートのはね返
りも少なくなり、コンクリートの損失量が少なくなる。
そして、作業環境も良くなる。更に又、通路管の接合面
を取はずし自在になるようにフランジ等の手段で接合す
ることにより、使用後の混合器内の洗浄が容易にでき
る。又、耐摩耗性を向上させるゴム、プラスチックス、
セラミックス等による被覆処理も容易にできる。本発明
による応用は、前述実施例に限らずに、緻密なコンクリ
ートを製造する混和剤や流動化剤、鉄筋のサビ止メ防止
の薬剤、吹付け工事で発生する粉塵の抑制剤等の添加混
合にも利用可能である。更に、樹脂モルタルの連続吹付
け工法、軽量気泡コンクリートの製造、下水汚泥の固
化、土砂のスラリー輸送、石炭と重油の混合燃料スラリ
ーの輸送等にも利用可能である。図5は、本発明の混合
器を利用した粒子径の違う鉄粉同士の混合に適用した場
合の概略系統図である。粒子径の違う鉄粉は、ホッパー
15及び16から粉体定量供給機17及び18を介し
て、各々の一定量を受けホッパー19に供給して、混合
器20内に重力落下で供給される。各々の鉄粉は混合器
20内を重力で落下しながら、通路管内に内設された螺
旋状の羽根体により、分割、合流、転位、せん断作用を
繰返しながら、連続的に撹拌混合される。本発明による
と、客先の仕様に合わせて、粒度分布の異なる鉄粉を、
短時間で、容易に、連続的に製造できる。この場合、原
料ホッパーを多数使用することで、多品種の粒度分布を
有する鉄粉の製造も容易にできる。又、混合の為の動力
を必要としないので省エネルギー効果も高く、混合器の
容積も小さくなる。更に、密閉系で連続的に混合できる
ので、粉塵の飛散による環境汚染の防止や混合物質の外
部からの汚染防止も可能となる。更に又、混合器内をテ
フロンライニングを行なうことで、付着性の強い粉粒体
の混合にも利用可能となる。なお、粉粒体の混合器への
供給方法は、重力落下方式のみでなく、空気輸送して混
合器に供給して、使用してもよい。
EXAMPLES Next, examples of the static fluid mixer according to the present invention will be described more specifically. FIG. 4 is a schematic system diagram when the static fluid mixer of the present invention is used for mixing concrete and a quick-setting admixture. cement,
Concrete consisting of gravel, water, etc. is pumped through the concrete pump 9 through the concrete supply line 10 into the static fluid mixer 14 by a fixed amount. On the other hand, the quick-setting agent that solidifies the concrete in a short time is pressure-fed into the mixer 14 from the quick-setting agent tank 11 through the quick-setting agent pump 12 and the quick-setting agent supply line 13. In the mixer 14, the concrete and the quick-setting agent that have been pressure-fed are continuously stirred and mixed by repeating the splitting, merging, shifting, and shearing actions by the spiral right and left twisted blade bodies 3 and 4 having openings. Thus, a mixed composition of homogeneous concrete and a setting agent can be produced. In this way, when applied to the mixing of concrete and the quick-setting admixture, the blade bodies 3 and 4 in the mixer 14 have a simple shape and therefore have a small flow resistance, and since there is no stagnation portion, the retention of concrete, There is no trouble due to blockage, and highly efficient mixing is possible. Furthermore, according to this manufacturing method, since the required amount can be mixed immediately before use, the loss of raw materials is reduced. When this mixed composition is used for spraying, it cures immediately after spraying. Therefore, the sprayed concrete layer can be thickly constructed, and the splashing of the concrete from the sprayed surface is reduced, so that the loss amount of the concrete is reduced.
And the working environment also improves. Furthermore, by joining with a means such as a flange so that the joining surface of the passage pipe can be removed, the inside of the mixer after use can be easily washed. In addition, rubber, plastics, which improve wear resistance,
The coating treatment with ceramics or the like can be easily performed. The application according to the present invention is not limited to the above-mentioned examples, but an admixture or a fluidizing agent for producing dense concrete, a chemical agent for preventing rusting of reinforcing bars, a chemical agent for suppressing dust generated during spraying work, etc. Is also available. Further, it can be used for continuous spraying method of resin mortar, production of lightweight cellular concrete, solidification of sewage sludge, transportation of slurry of earth and sand, transportation of mixed fuel slurry of coal and heavy oil. FIG. 5 is a schematic system diagram when applied to the mixing of iron powders having different particle diameters using the mixer of the present invention. The iron powders having different particle diameters are supplied from the hoppers 15 and 16 through the powder quantitative feeders 17 and 18 to the hoppers 19, respectively, and supplied to the hopper 19 by gravity drop. While each iron powder falls in the mixer 20 by gravity, it is continuously stirred and mixed by repeating the division, merging, dislocation, and shearing action by the spiral blade body provided in the passage tube. According to the present invention, according to the customer's specifications, iron powder with different particle size distribution,
It can be easily and continuously manufactured in a short time. In this case, by using a large number of raw material hoppers, it is possible to easily produce iron powder having a variety of particle size distributions. Further, since power for mixing is not required, the energy saving effect is high and the volume of the mixer is small. Furthermore, since the mixture can be continuously mixed in a closed system, it is possible to prevent environmental pollution due to dust scattering and prevent contamination of the mixed substance from the outside. Furthermore, by performing Teflon lining inside the mixer, it can be used for mixing powder particles having strong adhesion. In addition, the method of supplying the powdery or granular material to the mixer is not limited to the gravity drop method, but may be pneumatically transported and supplied to the mixer for use.

【0007】[0007]

【発明の効果】本発明によれば、高粘度物質、粉粒体、
コンクリート等の混合に利用でき、又、耐摩耗性、耐蝕
性に優れ、且つ、メインテナンスが容易な静止型流体混
合器を、低コストで製造できる。
INDUSTRIAL APPLICABILITY According to the present invention, a highly viscous substance, powder,
A static fluid mixer that can be used for mixing concrete and the like, has excellent wear resistance and corrosion resistance, and is easy to maintain can be manufactured at low cost.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の1実施例である静止型流体混合器の縦
断面図である。
FIG. 1 is a vertical sectional view of a static fluid mixer according to an embodiment of the present invention.

【図2】本発明の流体混合器のA−A線の断面図であ
る。
FIG. 2 is a sectional view taken along line AA of the fluid mixer of the present invention.

【図3】同じくB−B線の断面図である。FIG. 3 is a sectional view taken along line BB of FIG.

【図4】本発明の静止型流体混合器の適用例であるコン
クリートと急結剤との混合の系統図である。
FIG. 4 is a system diagram of mixing concrete and a quick-setting admixture, which is an application example of the static fluid mixer of the present invention.

【図5】同じく粒子径の異なる鉄粉の混合の系統図であ
る。
FIG. 5 is a system diagram of mixing of iron powders having different particle diameters.

【符号の説明】[Explanation of symbols]

1、14、20;静止型流体混合器 2、2a、2b;通路管 3、4;羽根体 5;スペース部 6、7;開口部 8;分割面 1, 14, 20; static fluid mixer 2, 2a, 2b; passage tubes 3, 4; blade body 5; space portion 6, 7; opening portion 8; split surface

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 流体が通流する通路管と、この通路管の
内周面に螺旋状に回転する複数個の羽根体とを配置した
ことを特徴とする静止型流体混合器。
1. A static fluid mixer comprising: a passage pipe through which a fluid flows; and a plurality of blades that spirally rotate on an inner peripheral surface of the passage pipe.
【請求項2】 前記通路管の内面及び羽根体の表面を、
ゴム、プラスチックス又はセラミックスで被覆したこと
を特徴とする請求項1に記載の静止型流体混合器。
2. The inner surface of the passage tube and the surface of the blade body are
The static fluid mixer according to claim 1, which is coated with rubber, plastics, or ceramics.
【請求項3】 長手方向に複数個に分割された前記通路
管の内周面に螺旋状の羽根体を接合する工程と、この通
路管の分割面同士を接合する工程とを有していることを
特徴とする静止型流体混合器の製造方法。
3. A step of joining a spiral blade to the inner peripheral surface of the passage tube divided into a plurality of pieces in the longitudinal direction, and a step of joining the divided surfaces of the passage tube. A method for manufacturing a static fluid mixer, comprising:
JP03290993A 1991-08-19 1991-08-19 Manufacturing method of static fluid mixer Expired - Fee Related JP3107877B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP03290993A JP3107877B2 (en) 1991-08-19 1991-08-19 Manufacturing method of static fluid mixer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP03290993A JP3107877B2 (en) 1991-08-19 1991-08-19 Manufacturing method of static fluid mixer

Publications (2)

Publication Number Publication Date
JPH0549887A true JPH0549887A (en) 1993-03-02
JP3107877B2 JP3107877B2 (en) 2000-11-13

Family

ID=17763073

Family Applications (1)

Application Number Title Priority Date Filing Date
JP03290993A Expired - Fee Related JP3107877B2 (en) 1991-08-19 1991-08-19 Manufacturing method of static fluid mixer

Country Status (1)

Country Link
JP (1) JP3107877B2 (en)

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11285628A (en) * 1998-04-02 1999-10-19 Matsushita Electric Ind Co Ltd Gas mixing device and production of gas discharge panel
EP1149626A1 (en) * 2000-04-27 2001-10-31 Sika AG, vorm. Kaspar Winkler & Co. Static mixing element, segment of a mixing element, static mixer and mixing blade and use thereof
JP2003038943A (en) * 2002-07-22 2003-02-12 Hisao Kojima Mixing element and manufacturing method therefor
KR100481930B1 (en) * 1996-04-12 2005-07-18 술저 켐테크 악티엔게젤샤프트 Low Viscosity Fluid Mixer Tubes
JP2006015762A (en) * 2005-09-27 2006-01-19 Denki Kagaku Kogyo Kk Blending device for cement concrete admixture
JP2006167718A (en) * 2004-12-16 2006-06-29 Hilti Ag Static mixer apparatus
JP2014040728A (en) * 2012-08-22 2014-03-06 Taiheiyo Material Kk Spray device for producing spray concrete
JP2015105493A (en) * 2013-11-29 2015-06-08 五洋建設株式会社 In-pipe agitation method of fluidized soil
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100481930B1 (en) * 1996-04-12 2005-07-18 술저 켐테크 악티엔게젤샤프트 Low Viscosity Fluid Mixer Tubes
JPH11285628A (en) * 1998-04-02 1999-10-19 Matsushita Electric Ind Co Ltd Gas mixing device and production of gas discharge panel
EP1149626A1 (en) * 2000-04-27 2001-10-31 Sika AG, vorm. Kaspar Winkler & Co. Static mixing element, segment of a mixing element, static mixer and mixing blade and use thereof
US6585407B2 (en) 2000-04-27 2003-07-01 Sika Schweiz Ag Static mixing element, single stage static mixing element segment, static mixer, mixing vanes element and method for mixing very viscous polyurethane with a curing accelerating agent
JP2003038943A (en) * 2002-07-22 2003-02-12 Hisao Kojima Mixing element and manufacturing method therefor
JP2006167718A (en) * 2004-12-16 2006-06-29 Hilti Ag Static mixer apparatus
JP2006015762A (en) * 2005-09-27 2006-01-19 Denki Kagaku Kogyo Kk Blending device for cement concrete admixture
JP2014040728A (en) * 2012-08-22 2014-03-06 Taiheiyo Material Kk Spray device for producing spray concrete
JP2015105493A (en) * 2013-11-29 2015-06-08 五洋建設株式会社 In-pipe agitation method of fluidized soil
JP2019084752A (en) * 2017-11-07 2019-06-06 株式会社神戸製鋼所 Mixing device
KR20200057079A (en) * 2017-11-07 2020-05-25 가부시키가이샤 고베 세이코쇼 Mixing device
US11944944B2 (en) 2017-11-07 2024-04-02 Kobe Steel, Ltd. Mixing apparatus

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