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JPS649045B2 - - Google Patents
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JPS649045B2 - - Google Patents

Info

Publication number
JPS649045B2
JPS649045B2 JP60141357A JP14135785A JPS649045B2 JP S649045 B2 JPS649045 B2 JP S649045B2 JP 60141357 A JP60141357 A JP 60141357A JP 14135785 A JP14135785 A JP 14135785A JP S649045 B2 JPS649045 B2 JP S649045B2
Authority
JP
Japan
Prior art keywords
valve
flow path
valve seat
liquid
pressure
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP60141357A
Other languages
Japanese (ja)
Other versions
JPS621444A (en
Inventor
Kozo Taneda
Takashi Kaneko
Sumio Ogawa
Shokei Chiba
Akira Sato
Toshiaki Ooshima
Hidetoshi Shimizu
Tetsuo Nakagawa
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.)
SANWA KIKAI KK
YUKIJIRUSHI NYUGYO KK
Original Assignee
SANWA KIKAI KK
YUKIJIRUSHI NYUGYO KK
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 SANWA KIKAI KK, YUKIJIRUSHI NYUGYO KK filed Critical SANWA KIKAI KK
Priority to JP60141357A priority Critical patent/JPS621444A/en
Publication of JPS621444A publication Critical patent/JPS621444A/en
Publication of JPS649045B2 publication Critical patent/JPS649045B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/44Mixers in which the components are pressed through slits
    • B01F25/441Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits
    • B01F25/4412Mixers in which the components are pressed through slits characterised by the configuration of the surfaces forming the slits the slits being formed between opposed planar surfaces, e.g. pushed again each other by springs
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01FMIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/40Static mixers
    • B01F25/44Mixers in which the components are pressed through slits
    • B01F25/442Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation
    • B01F25/4422Mixers in which the components are pressed through slits characterised by the relative position of the surfaces during operation the surfaces being maintained in a fixed but adjustable position, spaced from each other, therefore allowing the slit spacing to be varied

Landscapes

  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)

Description

【発明の詳細な説明】 (産業上の利用分野) 本発明はホモゲナイザー、すなわち高圧型均質
機に関するものである。
DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention relates to a homogenizer, that is, a high-pressure homogenizer.

(従来の技術) 一般的に、例えば、牛乳中の脂肪や蛋白質の粒
子を、物理的に細かく粉砕することにより、均一
な乳化状態をつくり出すことを均質化といい、か
かる均質化に用いられるものを高圧型均質機とい
う。従来の高圧型均質機は、第7図の如く弁座1
に形成された供給流路2から高圧液が供給され、
弁座1と弁3となす流路間隙4からブレーカーリ
ングー5に衝突し、弁スリーブ6を経て排出流路
7に排出されるようになつており、弁3は油圧ロ
ツド8とスプリング9とで往復動できるようにな
つている。又油圧シリンダー10中の油圧で作動
する。第7図中11は弁本体、12は油圧シリン
ダーカバーである。
(Prior art) Generally, for example, homogenization refers to creating a uniform emulsified state by physically finely pulverizing fat and protein particles in milk, and products used for such homogenization This is called a high-pressure homogenizing machine. The conventional high-pressure homogenizer has a valve seat 1 as shown in Figure 7.
High-pressure liquid is supplied from a supply channel 2 formed in
The fluid collides with the breaker ring 5 through the flow path gap 4 formed between the valve seat 1 and the valve 3, and is discharged through the valve sleeve 6 into the discharge flow path 7. It is designed to be able to move back and forth. It is also operated by the oil pressure in the hydraulic cylinder 10. In FIG. 7, 11 is a valve body, and 12 is a hydraulic cylinder cover.

(発明が解決しようとする問題点) 以上のような従来の均質機によれば、供給流路
2から液が弁3の外方にむかつて流れるので、弁
座の供給流路2側が流路面積が1番小さく圧力も
高い。そして、外方に行くにしたがつて、流路面
積が大きくなつていき、圧力も低くなつていく。
これは、流路間隙の摩擦状態を考慮すれば明らか
である。
(Problems to be Solved by the Invention) According to the conventional homogenizing machine as described above, since the liquid flows from the supply passage 2 toward the outside of the valve 3, the supply passage 2 side of the valve seat is connected to the flow passage. It has the smallest area and the highest pressure. As one goes outward, the area of the flow path becomes larger and the pressure becomes lower.
This becomes clear when considering the frictional state of the channel gap.

このため、流路間隙4から流出する急激な圧力
差は加圧圧力の約半分しかない。そして、加圧圧
力の約半分の圧力に対する流速でブレーカーリン
グー5に衝突して均質化が行われるものである。
Therefore, the sudden pressure difference flowing out from the channel gap 4 is only about half of the pressurizing pressure. Then, it collides with the breaker ring 5 at a flow rate corresponding to approximately half of the pressurizing pressure, and homogenization is performed.

したがつて、均質化を向上せしめようとすると
加圧圧力を大とせねばならない。
Therefore, in order to improve homogenization, the pressurizing pressure must be increased.

このように、加圧圧力を大とすることは、徒ら
に均質機が大きくなり、無駄にエネルギーを消費
するというきらいがある。
Increasing the pressurizing pressure in this manner has the disadvantage of unnecessarily increasing the size of the homogenizer and consuming energy unnecessarily.

(問題を解決するための手段) したがつて、本案の技術的課題は、加圧圧力を
大としなくとも均質化が向上するホモゲナイザー
すなわち高圧型均質機を提供しようとするもの
で、この技術的課題を解決する本案の技術的手段
は、弁と弁座とで外周から内方に向かう可調整自
在な供給流路間隙を形成すると共に、弁と弁座の
軸方向中心部のそれぞれに、互いに逆方向に分岐
する排出流路を形成して供給流路と排出流路とが
交叉する流路間隙において液の衝突が行われるべ
く構成し、かつ弁と弁座とのなす供給流路間隙に
は、断面山型の複数の凹凸部を形成して、この山
型部で液のキヤビテイシヨンが行われるべく構成
したものである。
(Means for solving the problem) Therefore, the technical problem of this proposal is to provide a homogenizer, that is, a high-pressure homogenizer that can improve homogenization without increasing the pressurizing pressure. The technical means of the present invention to solve the problem is to form a supply flow path gap between the valve and the valve seat that can be adjusted inward from the outer periphery, and to form a gap between the valve and the valve seat in the axial center of the valve and the valve seat. A discharge passage branching in opposite directions is formed so that liquid collision occurs in the passage gap where the supply passage and the discharge passage intersect, and the supply passage gap formed between the valve and the valve seat is In this method, a plurality of concave and convex portions having a chevron-shaped cross section are formed, and the liquid is cavitated at the chevron-shaped portions.

(発明の効果) 本発明によれば、次のような効果を奏するもの
である。すなわち、液の流れは従来のものでは弁
の中心から外方にむかつて流れるので、急激な圧
力差は加圧圧力の約半分しかない。
(Effects of the Invention) According to the present invention, the following effects are achieved. That is, in the conventional valve, the liquid flows outward from the center of the valve, so that the sudden pressure difference is only about half of the pressurizing pressure.

しかるに、本発明によれば、以上のような従来
と全く逆の流れとなり、弁の外方から弁の中心に
向かつて流れるようになつている。
However, according to the present invention, the flow is completely opposite to the conventional flow as described above, and flows from the outside of the valve toward the center of the valve.

したがつて、流路間隙における圧力降下は、流
れ抵抗のみで殆ど降下しない。このため加圧圧力
とほぼ同等な圧力差を得ることができる。そし
て、その加圧圧力に対する流速で且つ正面衝突と
なるため本来の衝撃の2倍の流速で衝突する。し
たがつて、均質効果が従来のものと比べて低い加
圧圧力で得られる。
Therefore, the pressure drop in the flow path gap is caused only by flow resistance and hardly drops. Therefore, a pressure difference substantially equivalent to the pressurizing pressure can be obtained. Then, since the collision occurs head-on, the collision occurs at a flow velocity corresponding to the applied pressure and at a flow velocity twice that of the original impact. Therefore, a homogeneous effect can be obtained at lower pressurizing pressures compared to conventional ones.

しかも、弁と弁座との間の流路間隙に形成され
た山型部では液が同圧力かつ流速を増しながら通
過し、均質効果の小さい外側から内側に向かつて
液が流れるので予備乳化の効果をだんだん高めて
いき、その後衝突で一気に均質化するということ
でバラツキの少ない均質効果がえられる。
Moreover, the liquid passes through the mountain-shaped part formed in the flow path gap between the valve and the valve seat with the same pressure and increasing flow velocity, and the liquid flows from the outside where the homogenizing effect is small to the inside, so that pre-emulsification is prevented. By gradually increasing the effect and then homogenizing it all at once through collision, a homogeneous effect with little variation can be obtained.

なお、従来のものでは、液がブレーカーリング
に衝突するため摩耗するが、本発明のものでは衝
突が液同志で起るため、衝突のための摩耗はな
く、そのエネルギーで均質効果を向上せしめると
いう特徴がある。
In addition, in the conventional type, the liquid collides with the breaker ring, causing wear, but in the case of the present invention, the collision occurs between the liquids, so there is no wear due to collision, and the homogeneity effect is improved by using the energy. It has characteristics.

(実施例) 以下図面に示す実施例について説明する。(Example) The embodiments shown in the drawings will be described below.

第1図において13は弁座であり、14はこれ
に対応する弁である。
In FIG. 1, 13 is a valve seat, and 14 is a corresponding valve.

弁座13と弁14の軸方向中心部にはそれぞれ
排出流路15,16が形成されている。
Discharge passages 15 and 16 are formed in the axial center of the valve seat 13 and the valve 14, respectively.

又、弁座13と弁14とで構成される可調整な
流路間隙(スリツト)17には、第4図の如く断
面山型の凹凸部18a,18bが形成され、山型
部18を構成している。
In addition, an adjustable flow path gap (slit) 17 formed by the valve seat 13 and the valve 14 is formed with uneven parts 18a and 18b having a chevron-shaped cross section as shown in FIG. are doing.

弁14と弁座13の周囲には、一定の間をおい
て弁スリーブ19があり、これに孔20がある。
Around the valve 14 and the valve seat 13 there is a valve sleeve 19 at a certain distance, in which a hole 20 is provided.

弁スリーブ19に対しては、供給流路21が開
口している。
A supply channel 21 opens into the valve sleeve 19 .

前記した排出流路15,16はそれぞれ弁本体
22に設けた環状流路23につながり合流して排
出口24から排出される。
The discharge passages 15 and 16 described above are connected to an annular passage 23 provided in the valve body 22, join together, and are discharged from the discharge port 24.

25は弁ロツドで、シリンダ27に孔30を介
して供給される油とスプリング26とで往復動
し、弁を押圧する。
A valve rod 25 is reciprocated by oil supplied to the cylinder 27 through a hole 30 and a spring 26 to press the valve.

なお、28は油圧シリンダーカバー、29は油
圧シリンダー本体である。
Note that 28 is a hydraulic cylinder cover, and 29 is a hydraulic cylinder main body.

第2,3図は弁スリーブの切断正面図と切断平
面図でリング状をなし、弁座13に当接する部分
には截頭突起19aがある。
2 and 3 are a cutaway front view and a cutaway plan view of the valve sleeve, which is ring-shaped and has a truncated projection 19a at the portion that abuts the valve seat 13.

第4図は、供給流路間隙における山型部の拡大
切断面図を示す。
FIG. 4 shows an enlarged cross-sectional view of the chevron-shaped portion in the supply channel gap.

さて、第1図により液が供給流路21から送ら
れると弁スリーブ19の孔20を通じて流路間隙
17の山型部18に送られ、ここで、同圧力で且
つ流速を増しながら通過する。したがつて、山型
部では予備乳化作用がえられる。
Now, as shown in FIG. 1, when the liquid is sent from the supply channel 21, it is sent through the hole 20 of the valve sleeve 19 to the chevron-shaped portion 18 of the channel gap 17, where it passes with the same pressure and increasing flow rate. Therefore, a preliminary emulsification effect can be obtained in the mountain-shaped portion.

そして、供給流路間隙17より通過した液同志
が正面衝突し、排出流路15,16へ流れる。
Then, the liquids passing through the supply channel gap 17 collide head-on and flow into the discharge channels 15 and 16.

液は、山型部での圧力降下は流れの抵抗のみで
殆ど降下せず加圧圧力と同等な圧力に対する流速
で正面衝突となるため、従来のものに比べて2倍
の流速で衝突する。
The liquid collides head-on at a flow velocity that is equivalent to the pressurized pressure, with almost no pressure drop at the mountain-shaped portion due to flow resistance, so the liquid collides at twice the flow velocity compared to the conventional one.

もつとも、流れの外側にいるものは多少衝撃が
弱くなるが、しかしその分キヤビテーシヨンが強
くなる。
Of course, those on the outside of the flow will receive a somewhat weaker impact, but the cavitation will be stronger accordingly.

この場合、排出流路16がないと液体の流れが
変わるので、液の中に真空状態が作られて好まし
くない。
In this case, if the discharge channel 16 is not present, the flow of the liquid will change, creating an undesirable vacuum state in the liquid.

何れにしても均質効果の少ない外側から内側へ
流れるので、予備乳化の効果をだんだんに高めて
いき、その後、衝突で一気に均質化するというこ
とでバラツキの少ない均質効果がえられる。
In any case, since the flow flows from the outside, where the homogenizing effect is low, to the inside, the preliminary emulsification effect is gradually increased, and then the homogenizing effect is achieved all at once by collision, thereby achieving a homogeneous effect with little variation.

かくて均質化された液は、排出流路15,16
に分岐して環状流路23から排出口24で合流し
て排出されるのである。
The thus homogenized liquid flows through the discharge channels 15 and 16.
The water is branched into the annular flow path 23, merges at the discharge port 24, and is discharged.

第5図は、弁と弁座の変型例を示すもので、弁
14における排出流路16の出口は開放でなく遮
断され、その代わり横方向に出口孔31が形成さ
れている。
FIG. 5 shows a modification of the valve and valve seat, in which the outlet of the discharge passage 16 in the valve 14 is not opened but is blocked, and instead an outlet hole 31 is formed in the lateral direction.

又、弁座13の排出流路15は等分に形成され
た傾斜状の放射溝32につながつている。
Further, the discharge passage 15 of the valve seat 13 is connected to an inclined radial groove 32 formed into equal parts.

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

第1図は本発明高圧型均質機の切断面図、第2
図は弁スリーブの切断面図、第3図は弁スリーブ
の切断平面図、第4図は山型部の拡大断面図、第
5,6図は弁座と弁の変型例を示す断面図と弁の
平面図、第7図は従来の高圧型均質機を示す切断
正面図である。 13……弁座、14……弁、15,16……排
出流路、17……供給流路間隙、18……山型
部、19……弁スリーブ、20……弁スリーブの
孔、21……供給流路。
Figure 1 is a cross-sectional view of the high-pressure homogenizer of the present invention, Figure 2
3 is a cutaway plan view of the valve sleeve, FIG. 4 is an enlarged sectional view of the chevron-shaped portion, and FIGS. 5 and 6 are sectional views showing modified examples of the valve seat and valve. A plan view of the valve, and FIG. 7 is a cutaway front view showing a conventional high-pressure homogenizer. 13... Valve seat, 14... Valve, 15, 16... Discharge channel, 17... Supply channel gap, 18... Chevron shaped portion, 19... Valve sleeve, 20... Hole in valve sleeve, 21 ...Supply channel.

Claims (1)

【特許請求の範囲】[Claims] 1 弁と弁座とで外周から内方に向かう可調整自
在な供給流路間隙を形成すると共に、弁と弁座の
軸方向中心部のそれぞれに、互いに逆方向に分岐
する排出流路を形成して供給流路と排出流路とが
交叉する流路間隙において液の衝突が行われるべ
く構成し、かつ弁と弁座とのなす供給流路間隙に
は、断面山型の複数の凹凸部を形成して、この山
型部で液のキヤビテイシヨンが行われるべく構成
したことを特徴とする高圧型均質機。
1. A supply flow path gap is formed between the valve and the valve seat that can be adjusted inward from the outer periphery, and a discharge flow path is formed in each of the axial centers of the valve and the valve seat that branches in opposite directions. The liquid is configured to collide with the liquid in the flow path gap where the supply flow path and the discharge flow path intersect, and the supply flow path gap formed between the valve and the valve seat has a plurality of uneven portions each having a chevron-shaped cross section. 1. A high-pressure homogenizing machine characterized by being configured so that cavitation of liquid is performed in this mountain-shaped portion.
JP60141357A 1985-06-27 1985-06-27 High pressure type homogenizer Granted JPS621444A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60141357A JPS621444A (en) 1985-06-27 1985-06-27 High pressure type homogenizer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60141357A JPS621444A (en) 1985-06-27 1985-06-27 High pressure type homogenizer

Publications (2)

Publication Number Publication Date
JPS621444A JPS621444A (en) 1987-01-07
JPS649045B2 true JPS649045B2 (en) 1989-02-16

Family

ID=15290095

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60141357A Granted JPS621444A (en) 1985-06-27 1985-06-27 High pressure type homogenizer

Country Status (1)

Country Link
JP (1) JPS621444A (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01152718U (en) * 1988-04-13 1989-10-20
JP2795513B2 (en) * 1990-02-27 1998-09-10 新日本製鐵株式会社 Decarburization refining method of chromium-containing molten steel
US5843334A (en) * 1994-06-20 1998-12-01 Nippon Shinyaku Co., Ltd. Method of producing emulsions and an emulsification apparatus
WO1996040423A1 (en) * 1995-06-07 1996-12-19 The Nutrasweet Company Apparatus and method for preparing colloidal dispersion
DE19905572A1 (en) * 1999-02-11 2000-08-31 Bayer Ag Device for mixing and reacting multiphase gaseous and liquid mixtures and use of this device
DE102022115580A1 (en) * 2022-06-22 2023-12-28 Hammelmann GmbH Homogenizing valve
IT202200023643A1 (en) * 2022-11-16 2024-05-16 Gea Mech Equipment Italia S P A A GUIDING DEVICE FOR GUIDING AN IMPACT HEAD AND A HOMOGENIZING VALVE COMPRISING SAID GUIDING DEVICE
EP4454742B1 (en) * 2022-11-16 2025-04-02 GEA Mechanical Equipment Italia S.p.A. A guiding device for guiding an impact head and a homogenizing valve comprising said guiding device

Also Published As

Publication number Publication date
JPS621444A (en) 1987-01-07

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