JPH01215238A - Method and apparatus for centrifugal removal of milk - Google Patents
Method and apparatus for centrifugal removal of milkInfo
- Publication number
- JPH01215238A JPH01215238A JP1015194A JP1519489A JPH01215238A JP H01215238 A JPH01215238 A JP H01215238A JP 1015194 A JP1015194 A JP 1015194A JP 1519489 A JP1519489 A JP 1519489A JP H01215238 A JPH01215238 A JP H01215238A
- Authority
- JP
- Japan
- Prior art keywords
- concentrate
- outlet
- drum
- milk
- nozzle
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 235000013336 milk Nutrition 0.000 title claims abstract description 24
- 239000008267 milk Substances 0.000 title claims abstract description 24
- 210000004080 milk Anatomy 0.000 title claims abstract description 24
- 238000000034 method Methods 0.000 title claims description 16
- 241000894006 Bacteria Species 0.000 claims abstract description 23
- 230000007246 mechanism Effects 0.000 claims abstract description 20
- 239000012141 concentrate Substances 0.000 claims description 83
- 230000001954 sterilising effect Effects 0.000 claims description 11
- 230000001105 regulatory effect Effects 0.000 claims description 9
- 238000004659 sterilization and disinfection Methods 0.000 claims description 6
- 239000004020 conductor Substances 0.000 claims description 2
- 230000000737 periodic effect Effects 0.000 claims 1
- 230000001580 bacterial effect Effects 0.000 description 18
- 238000000926 separation method Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 230000002093 peripheral effect Effects 0.000 description 5
- 230000035622 drinking Effects 0.000 description 4
- 230000002411 adverse Effects 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 235000020191 long-life milk Nutrition 0.000 description 3
- 235000020183 skimmed milk Nutrition 0.000 description 3
- 239000003925 fat Substances 0.000 description 2
- 235000013351 cheese Nutrition 0.000 description 1
- 235000013365 dairy product Nutrition 0.000 description 1
- 238000009795 derivation Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- JLQFVGYYVXALAG-CFEVTAHFSA-N yasmin 28 Chemical compound OC1=CC=C2[C@H]3CC[C@](C)([C@](CC4)(O)C#C)[C@@H]4[C@@H]3CCC2=C1.C([C@]12[C@H]3C[C@H]3[C@H]3[C@H]4[C@@H]([C@]5(CCC(=O)C=C5[C@@H]5C[C@@H]54)C)CC[C@@]31C)CC(=O)O2 JLQFVGYYVXALAG-CFEVTAHFSA-N 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C7/00—Other dairy technology
- A23C7/04—Removing unwanted substances other than lactose or milk proteins from milk
- A23C7/046—Removing unwanted substances other than lactose or milk proteins from milk by centrifugation without using chemicals, e.g. bactofugation; re-use of bactofugate
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B1/00—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles
- B04B1/10—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with discharging outlets in the plane of the maximum diameter of the bowl
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23C—DAIRY PRODUCTS, e.g. MILK, BUTTER OR CHEESE; MILK OR CHEESE SUBSTITUTES; MAKING THEREOF
- A23C2210/00—Physical treatment of dairy products
- A23C2210/25—Separating and blending
- A23C2210/256—Removal or separation of bacteria, or a fraction containing bacteria, by centrifugation; Bactofugation
-
- A—HUMAN NECESSITIES
- A63—SPORTS; GAMES; AMUSEMENTS
- A63F—CARD, BOARD, OR ROULETTE GAMES; INDOOR GAMES USING SMALL MOVING PLAYING BODIES; VIDEO GAMES; GAMES NOT OTHERWISE PROVIDED FOR
- A63F2300/00—Features of games using an electronically generated display having two or more dimensions, e.g. on a television screen, showing representations related to the game
- A63F2300/10—Features of games using an electronically generated display having two or more dimensions, e.g. on a television screen, showing representations related to the game characterized by input arrangements for converting player-generated signals into game device control signals
- A63F2300/1068—Features of games using an electronically generated display having two or more dimensions, e.g. on a television screen, showing representations related to the game characterized by input arrangements for converting player-generated signals into game device control signals being specially adapted to detect the point of contact of the player on a surface, e.g. floor mat, touch pad
- A63F2300/1075—Features of games using an electronically generated display having two or more dimensions, e.g. on a television screen, showing representations related to the game characterized by input arrangements for converting player-generated signals into game device control signals being specially adapted to detect the point of contact of the player on a surface, e.g. floor mat, touch pad using a touch screen
-
- A—HUMAN NECESSITIES
- A63—SPORTS; GAMES; AMUSEMENTS
- A63F—CARD, BOARD, OR ROULETTE GAMES; INDOOR GAMES USING SMALL MOVING PLAYING BODIES; VIDEO GAMES; GAMES NOT OTHERWISE PROVIDED FOR
- A63F2300/00—Features of games using an electronically generated display having two or more dimensions, e.g. on a television screen, showing representations related to the game
- A63F2300/30—Features of games using an electronically generated display having two or more dimensions, e.g. on a television screen, showing representations related to the game characterized by output arrangements for receiving control signals generated by the game device
- A63F2300/301—Features of games using an electronically generated display having two or more dimensions, e.g. on a television screen, showing representations related to the game characterized by output arrangements for receiving control signals generated by the game device using an additional display connected to the game console, e.g. on the controller
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Centrifugal Separators (AREA)
- Dairy Products (AREA)
- Physical Water Treatments (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、牛乳を遠心除菌する方法であって、牛乳を遠
心ドラムの供給部に供給し、該1心ドラムの濃縮物室中
では遠心分離された菌含有濃縮物が集積し、この濃縮物
のうち部分量をノズルを備えた導出通路を介して該遠心
ドラムから導出し、かつ残りの濃縮物をドラム外壁に設
けら口
れた搬出箋を介して周期的に搬出する形式のものに関す
る。さらに本発明は、上記方法を実施するための装置に
関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention provides a method for centrifugally sterilizing milk, in which milk is supplied to a feed section of a centrifugal drum, and in the concentrate chamber of the one-core drum. The centrifuged bacteria-containing concentrate is accumulated, a portion of this concentrate is drawn out of the centrifugal drum through a outlet passage provided with a nozzle, and the remaining concentrate is passed through a spout provided on the outer wall of the drum. It relates to a type of equipment that is periodically carried out via a carry-out note. Furthermore, the invention relates to a device for carrying out the above method.
このような形式の方法は公知であり、かつチーズ製造用
牛乳(K:a’sereimilch )および飲用牛
乳(Trinkmil、ch )を除菌するために使用
するのが有利である。この方法を実施するための適当な
遠心分離機は、たとえば西ドイツ国特許出願公告第29
13406号明細書から公知である。Processes of this type are known and are advantageously used for sterilizing cheese-making milk (K) and drinking milk (Trinkmil, ch 2 ). Suitable centrifuges for carrying out this process can be found, for example, in West German Patent Application No. 29
13406.
遠心ドラムの供給部を介して供給された牛乳量の約3チ
は、ノズルを備えた導出通路を介して菌含有濃縮物とし
て引出される。供給量の別の0.3チは、菌含有濃縮物
としてこの遠心ドラ口
ムの搬出孔を介して周期的に搬出される。こうして得ら
れた細菌濃縮物は、とりわけチーズ品質に不利な作用を
する菌株を含有する。したがって両部分流は再び合流せ
しめられ、特殊な滅菌装置中で熱処理にかけられ、その
際会ての菌株は死滅される。滅菌された濃縮物は次に再
び釜内牛乳(Kesselmilch )に添加するこ
とができる。しかしながら飲用牛乳を除菌する場合には
滅菌された細菌濃縮物を再び飲用牛乳中に戻すことは許
されていないので、生じる細菌濃縮物量は飲用牛乳を製
造する場合には失なわれる。Approximately 3 inches of the milk quantity supplied via the feed section of the centrifugal drum is withdrawn as bacteria-containing concentrate via a discharge channel equipped with nozzles. Another 0.3 g of the feed is periodically discharged as bacteria-containing concentrate via the discharge hole of this centrifugal drum. The bacterial concentrate thus obtained contains, inter alia, bacterial strains that have an adverse effect on cheese quality. The two partial streams are then combined again and subjected to a heat treatment in a special sterilization device, in which case the combined bacterial strains are killed. The sterilized concentrate can then be added back to the kettle milk. However, when sterilizing drinking milk, it is not allowed to reintroduce the sterilized bacterial concentrate into the drinking milk, so that the amount of bacterial concentrate produced is lost when producing the drinking milk.
それどころか、滅菌された細菌濃縮物を乳製品に添加す
ることを原則的に禁止しようとする動きさえある。その
場合、この細菌濃縮物は支払い額の劣る飼料として使用
することができるにすぎなくなる。In fact, there are even moves to ban the addition of sterilized bacterial concentrates to dairy products in principle. This bacterial concentrate can then only be used as low-paying feed.
本発明の課題は、生じる細菌濃縮物量を著しく減少させ
ることのできる、牛乳を遠心除菌する方法を提供するこ
とである@
〔課題を解決するための手段〕
上記の課題は、ノズルを介して導出される濃細物な濃縮
物室の中央範囲から引出し、遠心ドラムの供給部に戻す
ことにより解決される。The problem of the present invention is to provide a method for centrifugal sterilization of milk, which makes it possible to significantly reduce the amount of bacterial concentrate produced. This is achieved by withdrawing the concentrate from the central region of the concentrate chamber and returning it to the supply of the centrifugal drum.
意外にも、本発明による方法を用いれば流出する除菌牛
乳の品質に不利な影響を及ぼすことなしに、ノズルを介
して導出された全濃縮物量を供給部に戻すことが可能で
あることが判明した。Surprisingly, it has been found that, using the method according to the invention, it is possible to return the entire concentrate quantity drawn off via the nozzle to the feed without adversely affecting the quality of the sterilized milk flowing out. found.
このことは、ノズルを介して導出される部分量が、濃縮
物室のたんに僅少量の細菌しか存在しない中央範囲から
引出されることに基づいている。すなわち、濃縮物中に
含まれている細菌は特に搬出口付近のドラム周壁に集積
するが、この濃縮物の残りの成分、脂肪およびタンパク
質は導出通路およびノズルを経由する進路を取るので、
流入する牛乳中で返送により菌数の重大な増加が生じる
ことはない。これにより、除菌された牛乳中での菌数の
予想しうる増加は起こらない。This is based on the fact that the portion delivered via the nozzle is drawn from the central region of the concentrate chamber, where only a small amount of bacteria is present. That is, while the bacteria contained in the concentrate accumulates particularly on the peripheral wall of the drum near the outlet, the remaining components of this concentrate, fats and proteins, take their path through the outlet passage and nozzle.
Returns do not result in a significant increase in bacterial counts in the incoming milk. This does not result in a predictable increase in the number of bacteria in the sterilized milk.
ノズルを介して導出される部分量が導出される範囲は、
−面においてできるだけ僅かな細菌含分な有する脱脂乳
が引出され、他面においてなお脂肪粒子が一緒に取除か
れてしまわないように選択すべきである。そうでなけれ
ば、この脱脂乳は損なわれしまうであろう。The range in which the partial quantities delivered via the nozzle are derived is
The choice should be made such that skimmed milk with as low a bacterial content as possible is drawn off on the - side, while still not allowing fat particles to be removed along with the other side. Otherwise, this skimmed milk would be spoiled.
公知の遠心ドラムの場合、生じる菌含有濃縮物の両部分
量は濃縮物室の周壁から引出される。In the case of known centrifugal drums, both partial volumes of the resulting bacteria-containing concentrate are drawn off from the peripheral wall of the concentrate chamber.
したがって両部分量は高い細菌濃度を有する。Both portions therefore have high bacterial concentrations.
それ故に、ノズルを備えた導出通路を介して引出された
部分量を遠心Pラムの供給部に返送することは、遠心分
離器の流出部中の細菌濃度を除々に増大させ、ひいては
除菌された牛乳の品質に不利な影響を及ぼす恐れがある
。Therefore, returning the drawn-off part quantity via the outlet channel equipped with a nozzle to the supply of the centrifugal P ram gradually increases the bacterial concentration in the outlet of the centrifuge, and thus the sterilized This may have an adverse effect on the quality of milk produced.
ノズルに通じる通路を濃縮物室の中央範囲から出発させ
、これによりほとんど無菌の脱脂乳を引出すようにする
ことは、遠心ドラムの分離効果に対して不都合なしに可
能であることが確認された。すなわちこの部分量の引出
しは、濃縮物室中で細菌に対して吸引作用を行使する目
的で、これらの細菌がこの濃縮物室の周壁に移動するよ
うにするために必要であるにすぎない。It has been found possible to have the passage leading to the nozzle start from the central area of the concentrate chamber, thereby drawing off almost sterile skim milk, without any disadvantage to the separation effect of the centrifugal drum. The withdrawal of this partial quantity is therefore only necessary in order to exert a suction effect on the bacteria in the concentrate chamber so that these bacteria migrate to the peripheral wall of this concentrate chamber.
この吸引作用なしでは、分離効果は著しく劣悪となる。Without this suction effect, the separation effect would be significantly poorer.
本発明の有利な1構成の場合、ノズルを介して導出され
た濃縮物は2つの部分流に分割され、そのうち第1部分
流は遠心Pラムの供給部に戻され、第2部分流は搬出口
から流出する濃縮物と合流せしめられ、その際この第2
部分流の量は搬出口から流出する濃縮物量に応じて、こ
の合流後に一定出力の濃縮物流が生じるように調節され
る。このことは後接された滅菌工程のために有利である
。それというのも、この滅菌工程には一定の出力が供給
されなければならないからである。したがって、これら
の変動量を捕集するためのこれまで必要とされた相応に
大きな積重ね容器は不要とすることができる。In one advantageous embodiment of the invention, the concentrate discharged via the nozzle is divided into two partial streams, of which the first partial stream is returned to the feed of the centrifugal P ram and the second partial stream is conveyed. The concentrate flowing out from the outlet is merged with this second
The amount of the partial stream is adjusted depending on the amount of concentrate exiting the outlet so that after this merging, a constant output concentrate stream is produced. This is advantageous for the subsequent sterilization step. This is because a constant power must be supplied to this sterilization process. Accordingly, the correspondingly large stacks of containers required hitherto to collect these fluctuations can be dispensed with.
遠心ドラムの搬出口から噴出される濃縮物量が全濃縮物
量のわずか約10%であるにすぎないので、一定の容量
流を発生させるためKは戻り導管から小さな部分流を分
岐させるだけで十分である。Since the concentrate volume emerging from the outlet of the centrifugal drum is only about 10% of the total concentrate volume, it is sufficient for K to branch off a small partial stream from the return conduit in order to generate a constant volumetric flow. be.
本発明方法の他の有利な構成は請求項3または4に記載
されている。Further advantageous developments of the method according to the invention are specified in claim 3 or 4.
本発明方法を実施するための装置ならびにその有利な構
成は、請求項5から9までのいずれか1項に記載されて
いる。A device for carrying out the method according to the invention as well as advantageous embodiments thereof is defined in one of the claims 5 to 9.
本発明の1実施例は図面に示されており、次にこれを詳
説する。An embodiment of the invention is shown in the drawings and will now be described in detail.
第1図には1で遠心ドラムが示されており、この遠心ド
ラムの流入室2は通路3を介して分離板組4と連通して
おり、この分離板組は濃縮物室5を半径方向に内向きで
制限する。この濃縮物室5からは、ノズルTを備えた導
出通路6が導出室8に通じており、この導出室中には導
出機構9が存在し、この導出室の濃縮物流出部10は戻
り導管11を介して、遠心ドラム1の流入室2中に開口
する供給部12と連通している。ドラム周壁からはピス
トンスライダ13によって開放すべき搬出口14が、細
菌濃縮物のための捕集客器15に通じている。戻り導管
11には返送すべき細菌濃縮物量を調節するための調節
機構16が設けられている。導出通路6はドラムカバー
17と、遠心ドラム1中でこのカバーに対して間隔”A
”を保って設けられた、リブ19を備えた円錐導出板1
8との間に形成される。除菌された牛乳は通路20を介
して導出室21に流入し、次いで導出機構22によりさ
らに流出部23に案内される。FIG. 1 shows a centrifugal drum at 1, the inlet chamber 2 of which communicates via a passage 3 with a set of separator plates 4, which separates a concentrate chamber 5 in a radial direction. Limit yourself inwardly. From this concentrate chamber 5, a discharge channel 6 with a nozzle T leads to a discharge chamber 8, in which a discharge mechanism 9 is present, and a concentrate outlet 10 of this discharge chamber is connected to a return conduit. Via 11, it communicates with a feed 12 which opens into the inlet chamber 2 of the centrifugal drum 1. A discharge opening 14, which is opened by a piston slide 13, from the drum peripheral wall leads to a collection container 15 for the bacterial concentrate. The return conduit 11 is provided with a regulating mechanism 16 for regulating the amount of bacterial concentrate to be returned. The outlet channel 6 is connected to the drum cover 17 at a distance "A" with respect to this cover in the centrifugal drum 1.
Conical lead-out plate 1 with ribs 19 provided while maintaining the
8. The sterilized milk flows into the outlet chamber 21 through the passage 20, and is then further guided to the outlet 23 by the outlet mechanism 22.
除菌すべき牛乳は供給部12を介してこの遠心ドラムに
供給され、かつ流入室2および通路3を介して分離板組
4に流入し、この分離板組中では細菌が牛乳と分離され
、次いでこれらの菌は濃縮物室5へ移動する。The milk to be sterilized is fed to this centrifugal drum via a feed 12 and flows via an inlet chamber 2 and a passage 3 into a separating plate set 4 in which bacteria are separated from the milk. These bacteria then move to the concentrate chamber 5.
導出通路6およびノズル7を介して、菌貧有の濃縮物の
部分流が遠心ドラムの濃縮物室5から不断に導出され、
かつ導出機構9、濃縮物流出部10ならびに戻り導管1
1を介して遠心ドラム1の供給部12に返送される。ド
ラム周壁に集積する細菌は、搬出口14を介して周期的
にこの遠心ドラム1から搬出される。Via the outlet channel 6 and the nozzle 7, a partial stream of the bacteria-poor concentrate is continuously drawn off from the concentrate chamber 5 of the centrifugal drum;
and a discharge mechanism 9, a concentrate outlet 10 and a return conduit 1.
1 to the supply section 12 of the centrifugal drum 1. Bacteria accumulated on the peripheral wall of the drum are periodically transported out of the centrifugal drum 1 via the exit port 14.
ノズル7を備えた導出通路6は、濃縮物室5の半径方向
に見てその中央範囲から延びている。A discharge channel 6 with a nozzle 7 extends from the radially central region of the concentrate chamber 5 .
これにより、特に菌貧有の濃縮物が濃縮物室5から引出
されるので、遠心ドラム1の供給部12中で菌数が増加
する危険は回避される。As a result, particularly bacteria-poor concentrate is withdrawn from the concentrate chamber 5, so that the risk of an increase in the number of bacteria in the supply section 12 of the centrifugal drum 1 is avoided.
ドラムカバー17と円錐導出板18との間の間隔”A”
は、この間隔から生じる導出通路6中での菌含有濃縮物
の流速においてこの導出通路中でなお付加的な細菌分離
が行なわれるように選択されている。導出通路6中で作
用するコリオリの力のため、この導出通路6の横断面に
関係なく十分な間隔”A″が必要である。この間隔”A
″を、個々の導出通路6に対して間隔”A”1flあた
り約15J/hの処理能力が得られるように選択した場
合、良好な結果が得られた。たとえば遠心ドラムに20
0001/hの菌含有牛乳を供給し、そのうちの5%を
菌含有濃縮物として8個のリブ19によって形成される
導出通路6を介して引出す場合には、この導出通路61
つにっき;
200001/hxO,05: 8=1 25A’/h
の処理能力が得られる。Distance “A” between drum cover 17 and conical lead-out plate 18
is selected such that at the flow rate of the bacteria-containing concentrate in the outlet channel 6 resulting from this distance, an additional bacterial separation still takes place in this outlet channel. Due to the Coriolis forces acting in the outlet channel 6, a sufficient spacing "A" is necessary regardless of the cross section of this outlet channel 6. This interval “A”
Good results have been obtained when ``A'' is selected in such a way that a throughput of approximately 15 J/h per fl of interval ``A'' is obtained for the individual outlet channels 6.For example, 20
0001/h of milk containing bacteria is supplied, and when 5% of it is drawn out as a bacteria-containing concentrate through the outlet passage 6 formed by eight ribs 19, this outlet passage 61
Nikki; 200001/hxO,05: 8=1 25A'/h
processing power can be obtained.
との値を間隔”A”1nにつき目標とされる151/h
で除すると、間隔″′A”は8.33flと計算される
。The value of 151/h is targeted for interval "A" 1n.
The interval "'A" is calculated to be 8.33fl.
戻り導管11の調節機構16により、導出通路を介して
引出すべき濃縮物量は容易に調節することができる。By means of the adjustment mechanism 16 of the return conduit 11, the amount of concentrate to be drawn off via the outlet channel can be easily adjusted.
生じる菌含有濃縮物量を小さく保つためには、搬出口を
介して搬出される濃縮物量が供給量の最大0.4〜0.
6チであると望ましい。In order to keep the amount of bacteria-containing concentrate produced small, the amount of concentrate discharged via the discharge port must be at most 0.4 to 0.0% of the supply amount.
It is desirable that it is 6 inches.
第2図によれば、細菌のより良好な後分離を行なうため
に、ドラムカバー17と円錐導出板18との間に後分離
板24が設けられている。According to FIG. 2, a post-separation plate 24 is provided between the drum cover 17 and the conical outlet plate 18 in order to achieve a better post-separation of the bacteria.
第3図に示された装置の場合、戻り導管11から濃縮物
導管36が、この濃縮物導管36と搬出口14とを介し
て導出された濃縮物を合流させるための合流装置25に
通じている0この合流装置25には調節装置26が所属
しており、この調節装置は導線27,28および制御装
置29を介して調節機構16および濃縮物導管36中の
調節機構30と接続している。合流装置25には調節可
能なポンプ31が接続されており、このポンプは合流装
置25から細菌濃縮物を一定の出力で排出し、引き続き
滅菌装置(図示せず)に圧送する。In the case of the device shown in FIG. 3, a concentrate conduit 36 leads from the return conduit 11 to a merging device 25 for merging the concentrate discharged via this concentrate conduit 36 and the outlet 14. A regulating device 26 is assigned to this merging device 25, which is connected via lines 27, 28 and a control device 29 to the regulating device 16 and to the regulating device 30 in the concentrate line 36. . An adjustable pump 31 is connected to the merging device 25, which pumps the bacterial concentrate from the merging device 25 with a constant output and subsequently pumping it to a sterilization device (not shown).
ノズル7を介して排出された細菌濃縮物の部分流は、濃
縮物導管36を介して合流装置25に流入し、この合流
装置中では搬出口14を介して噴出された濃縮物も捕集
される。合流装置25中の液面に応じて調節機構16.
3Gは調節装置26および制御装置29により、この合
流装置25中の液面が本質的に変化しないように調節さ
れる。手動式の調節機構32.33を用いて基準量調節
を行なうことができる。調節機構30が完全に開いてい
るにもかかわらず合流装置25中の液面が許容しえない
程度に低下する場合、濃縮物導管36の基準量調節は調
節機構34を備えたバイパス導管35により超過させる
ことができる。調節機構32.33および34を使用す
る場合、制御装置によって操作される調節機構16.3
0および34はリモートコントロール式の簡単な遮断機
構として構成されていてよく、これにより特に安価な調
節可能性が得られる。The partial stream of the bacterial concentrate discharged via the nozzle 7 flows via the concentrate conduit 36 into the combining device 25 in which the concentrate ejected via the outlet 14 is also collected. Ru. Adjustment mechanism 16 depending on the liquid level in the merging device 25.
3G is regulated by the regulating device 26 and the control device 29 in such a way that the liquid level in this merging device 25 remains essentially unchanged. Manual adjustment mechanisms 32,33 can be used to perform the reference amount adjustment. If the liquid level in the merging device 25 drops to an unacceptable degree despite the adjustment mechanism 30 being fully open, the reference volume adjustment of the concentrate conduit 36 is carried out by means of the bypass conduit 35 with the adjustment mechanism 34. can be exceeded. When using adjustment mechanisms 32.33 and 34, adjustment mechanism 16.3 operated by the control device
0 and 34 can be configured as a simple remote-controlled shut-off mechanism, which provides particularly inexpensive adjustment possibilities.
図面は本発明の1実施例を示すものであって、第1図は
遠心ドラムの略示縦断面図、第2図は第1図による”X
”範囲の詳細図、第3図は戻り導管からの部分流と搬出
口から噴出された細菌濃縮物とを混合する装置の回路図
である。
1・・・遠心ドラム、2・・・流入室、3・・・通路、
4・・・分離板組、5・・・濃縮物室、6・・・導出通
路、7・・・ノズル、8・・・導出室、9・・・導出機
構、10・・・濃縮物流出部、11・・・戻り導管、1
2・・・供給部、13・・・ピストンスライダ、14・
・・搬出口、15・・・捕集容器、16・・・導出通路
、17・・・ドラムカバー、18・・・円錐導出板、1
9・・・リブ、20・・・通路、21・・・導出室、2
2・・・導出機構、23・・・流出部、24・・・後分
離板、25・・・合流装置、27.28・・・導線、2
9・・・制御装置、30・・・調節機構、31・・・ポ
ンプ、32.33.34・・・調節機構、35・・・バ
イパス導管、36・・・濃縮物導管、A・・・間隔The drawings show one embodiment of the present invention, in which FIG. 1 is a schematic vertical sectional view of a centrifugal drum, and FIG.
3 shows a circuit diagram of the device for mixing the partial flow from the return conduit with the bacterial concentrate ejected from the outlet. 1. Centrifugal drum, 2. Inlet chamber. , 3...Aisle,
4... Separation plate set, 5... Concentrate chamber, 6... Outlet passage, 7... Nozzle, 8... Outlet chamber, 9... Outlet mechanism, 10... Concentrate outflow Part, 11...Return conduit, 1
2... Supply section, 13... Piston slider, 14.
... Carrying out port, 15... Collection container, 16... Outlet passage, 17... Drum cover, 18... Conical outlet plate, 1
9... Rib, 20... Passage, 21... Lead-out chamber, 2
2... Derivation mechanism, 23... Outflow section, 24... Rear separation plate, 25... Merging device, 27.28... Conductor, 2
9... Control device, 30... Adjustment mechanism, 31... Pump, 32.33.34... Adjustment mechanism, 35... Bypass conduit, 36... Concentrate conduit, A... interval
Claims (1)
ムの供給部に供給し、該遠心ドラムの濃縮物室中では遠
心分離された菌含有濃縮物が集積し、この濃縮物のうち
部分量をノズルを備えた導出通路を介して該遠心ドラム
から導出し、かつ残りの濃縮物をドラム外壁に設けられ
た搬出口を介して周期的に搬出する形式のものにおいて
、ノズルを介して導出される濃縮物を濃縮物室の中央範
囲から引出し、かつ遠心ドラムの供給部に戻すことを特
徴とする、牛乳を遠心除菌する方法。 2、ノズルを介して導出された濃縮物を2つの部分流に
分け、第1部分流を遠心ドラムの供給部に戻し、かつ第
2部分流を搬出口から流出する濃縮物と合流させ、その
際この第2部分流の量を搬出口から流出する濃縮物量に
応じて、この合流後に一定出力の濃縮物が生じるように
調節する、請求項1記載の方法。 3、ノズルを介して引出される濃縮物量が、遠心ドラム
の供給部を介して供給された牛乳量の最大1〜10%で
ある、請求項1または2記載の方法。 4、遠心ドラムの搬出口を介して搬出される濃縮物量が
、該遠心ドラムの供給部を介して供給された牛乳量の0
.1〜1.0%である、請求項1から3までのいずれか
1項記載の方法。 5、請求項1記載の方法を実施するための装置であつて
遠心ドラム(1)が供給部(12)および分離板組(4
)を備え、該分離板組が濃縮物室(5)を半径方向に内
向きで制限し、かつこの濃縮物室からはノズル(7)を
備えた導出通路(6)ならびに周期的な濃縮物搬出のた
めの搬出口(14)が延びており、前記ノズル(7)が
導出室(8)に開口し、この導出室中には前記ノズルを
介して引出された菌貧有の濃縮物を濃縮物流出部(10
)中に圧送するための導出機構(9)が設けられている
形式のものにおいて、前記導出通路 (6)が、濃縮物室(5)の半径方向に見てその中央範
囲から延びており、かつ前記濃縮物流出部(10)が戻
り導管(11)を介して遠心ドラム(1)の供給部(1
2)と結合されていることを特徴とする、牛乳を遠心除
菌する装置。 6、戻り導管(11)から調節機構(30)を備えた濃
縮物導管(36)が分岐されており、かつこの濃縮物導
管(36)を介して導出された濃縮物と、搬出口(14
)を介して導出された濃縮物とを合流させるための合流
装置(25)が設けられており、該合流装置(25)に
は合流された濃縮物流の一定の容量流を調節するための
調節装置(26)が相互配置されており、この調節装置
が導線(27、28)および制御装置(29)を介して
濃縮物導管(36)中の調節機構(30)および戻り導
管(11)中の調節機構(16)と接続している、請求
項5記載の装置。 7、導出通路(6)がドラムカバー(17)と、遠心ド
ラム中でこのドラムカバーに対して間隔“A”を保つて
設けられた円錐導出板(18)との間に配置されている
リブ(19)により形成されている、請求項5または6
記載の装置。 8、間隔“A”は、リブ(19)によつて形成されたそ
れぞれ個々の導出通路(6)に対して該間隔“A”1m
mにつき5〜25l/hの処理能力が得られるように選
択されている、請求項7記載の装置。 9、ドラムカバー(17)と円錐導出板(18)との間
に後分離板(24)が設けられている、請求項7または
8記載の装置。[Scope of Claims] 1. A method for centrifugally sterilizing milk, in which milk is supplied to a supply section of a centrifugal drum, and a centrifuged concentrate containing bacteria is accumulated in a concentrate chamber of the centrifugal drum. , a type in which a portion of this concentrate is led out of the centrifugal drum through a lead-out passage equipped with a nozzle, and the remaining concentrate is periodically taken out through a discharge port provided on the outer wall of the drum. A method for centrifugal sterilization of milk, characterized in that the concentrate discharged via the nozzle is withdrawn from the central region of the concentrate chamber and returned to the feed of the centrifugal drum. 2. Dividing the concentrate discharged through the nozzle into two partial streams, returning the first partial stream to the feed of the centrifugal drum, and merging the second partial stream with the concentrate exiting from the outlet; 2. The method as claimed in claim 1, wherein the amount of this second partial stream is adjusted as a function of the amount of concentrate exiting the outlet so that a constant output of concentrate results after this combination. 3. Process according to claim 1 or 2, characterized in that the amount of concentrate drawn off via the nozzle is at most 1-10% of the amount of milk fed via the feed of the centrifugal drum. 4. The amount of concentrate discharged through the discharge port of the centrifugal drum is equal to or less than the amount of milk supplied through the supply section of the centrifugal drum.
.. 4. A method according to any one of claims 1 to 3, wherein the amount is between 1 and 1.0%. 5. An apparatus for carrying out the method according to claim 1, wherein the centrifugal drum (1) comprises a supply section (12) and a separator plate set (4).
), the separator plate set radially inwardly delimiting a concentrate chamber (5), from which a discharge channel (6) with a nozzle (7) as well as a periodic concentrate chamber are provided. A discharge opening (14) for discharge extends, and said nozzle (7) opens into a discharge chamber (8) into which the bacteria-poor concentrate drawn out via said nozzle is deposited. Concentrate outlet (10
), in which said outlet passageway (6) extends from the radially central area of the concentrate chamber (5); and said concentrate outlet (10) is connected via a return conduit (11) to the supply section (1) of the centrifugal drum (1).
An apparatus for centrifugally sterilizing milk, characterized in that it is combined with 2). 6. A concentrate conduit (36) equipped with an adjustment mechanism (30) is branched from the return conduit (11), and the concentrate discharged through this concentrate conduit (36) and the outlet (14) are separated from each other.
A merging device (25) is provided for merging the concentrates drawn off via the The devices (26) are arranged in relation to each other, the regulating device being connected via the conductors (27, 28) and the control device (29) to the regulating mechanism (30) in the concentrate conduit (36) and in the return conduit (11). 6. The device according to claim 5, wherein the device is connected to an adjustment mechanism (16) of. 7. A rib in which the outlet passage (6) is arranged between the drum cover (17) and a conical outlet plate (18) provided in the centrifugal drum at a distance "A" with respect to this drum cover. Claim 5 or 6 formed by (19)
The device described. 8. The distance "A" is 1 m for each individual outlet passageway (6) formed by a rib (19).
8. The device according to claim 7, wherein the device is selected to provide a throughput of 5 to 25 l/h per m. 9. Device according to claim 7 or 8, characterized in that a rear separating plate (24) is provided between the drum cover (17) and the conical outlet plate (18).
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE3802305A DE3802305C1 (en) | 1988-01-27 | 1988-01-27 | Process and apparatus for the centrifugal removal of bacteria from milk |
DE3802305.9 | 1988-01-27 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01215238A true JPH01215238A (en) | 1989-08-29 |
JPH0412933B2 JPH0412933B2 (en) | 1992-03-06 |
Family
ID=6346056
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1015194A Granted JPH01215238A (en) | 1988-01-27 | 1989-01-26 | Method and apparatus for centrifugal removal of milk |
Country Status (11)
Country | Link |
---|---|
JP (1) | JPH01215238A (en) |
AR (1) | AR241624A1 (en) |
AT (1) | AT396049B (en) |
BR (1) | BR8900326A (en) |
CH (1) | CH675667A5 (en) |
DE (1) | DE3802305C1 (en) |
DK (1) | DK175463B1 (en) |
FR (1) | FR2626143B1 (en) |
IE (1) | IE62885B1 (en) |
IT (1) | IT1224035B (en) |
NL (1) | NL188202C (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013504335A (en) * | 2009-09-16 | 2013-02-07 | ジーイーエー メカニカル エクイップメント ゲーエムベーハー | Method for producing raw milk that can be stored for a relatively long period of time |
WO2013069546A1 (en) * | 2011-11-07 | 2013-05-16 | テトラ ラバル ホールディングス アンド ファイナンス エス エイ | Method for producing and device for producing cheese starting material milk |
WO2013069547A1 (en) * | 2011-11-07 | 2013-05-16 | テトラ ラバル ホールディングス アンド ファイナンス エス エイ | Method for producing and device for producing starting material milk for skim milk |
Families Citing this family (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4040294C2 (en) * | 1990-12-17 | 1994-06-16 | Westfalia Separator Ag | Self-draining centrifugal drum for sterilizing milk |
DK169510B1 (en) * | 1993-05-13 | 1994-11-14 | Apv Pasilac As | Plant and method of treating milk |
DE4322415C2 (en) * | 1993-07-06 | 1996-11-28 | Westfalia Separator Ag | Centrifugal drum to concentrate suspended solids |
DE19503065C1 (en) * | 1995-02-01 | 1995-11-30 | Westfalia Separator Ag | Centrifugal sterilising of milk with minimised waste |
DE19540031C1 (en) * | 1995-10-27 | 1997-03-13 | Westfalia Separator Ag | Centrifuge drum for concentrating solids with outlets to stripping chamber |
DE19955178B4 (en) * | 1999-11-16 | 2004-12-23 | Tetra Pak Processing Gmbh | Process and plant for the treatment of centrifugal sediment from separators |
DE10135317A1 (en) * | 2001-07-19 | 2003-01-30 | Bayer Ag | Deflection ring for a self-discharging centrifuge |
CN111511474B (en) * | 2017-12-19 | 2022-06-07 | 利乐拉瓦尔集团及财务有限公司 | Separator and method for separating milk |
KR102296235B1 (en) * | 2021-04-22 | 2021-08-31 | 주식회사 삼공사 | Thin Disc Stack Centrifugal Oil Mist Separator |
CN116764824B (en) * | 2023-08-25 | 2023-11-07 | 山东万佳食品有限公司 | Centrifuge for monosodium glutamate production |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63252560A (en) * | 1987-03-19 | 1988-10-19 | アルフア−ラヴアル セパレーシヨン アーベー | Centrifugal separator |
Family Cites Families (7)
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GB307933A (en) * | 1928-03-17 | 1929-10-17 | Separator Ab | Improvements in or relating to the centrifugal cleaning of liquids |
US3217982A (en) * | 1958-10-17 | 1965-11-16 | Westfalia Separator Ag | Apparatus for the sterilization of liquids |
NL128342C (en) * | 1966-11-22 | |||
DE2913406B1 (en) * | 1979-04-04 | 1980-08-28 | Westfalia Separator Ag | Centrifugal drum with vertical axis of rotation for concentration of suspensions |
DE3314859A1 (en) * | 1983-04-23 | 1984-10-25 | Westfalia Separator Ag, 4740 Oelde | METHOD AND DEVICE FOR CENTRIFUGAL CLEANING OF USED MINERAL OILS |
DE3601814A1 (en) * | 1986-01-22 | 1987-07-23 | Westfalia Separator Ag | METHOD AND DEVICE FOR SEPARATING TWO LIQUID PHASES BY MEANS OF A CENTRIFUGE |
DE3620548A1 (en) * | 1986-06-19 | 1987-12-23 | Westfalia Separator Ag | METHOD AND DEVICE FOR PRODUCING CITRUS JUICES WITH A LOW REMAINING PUMP |
-
1988
- 1988-01-27 DE DE3802305A patent/DE3802305C1/en not_active Expired
- 1988-11-25 AT AT0290488A patent/AT396049B/en not_active IP Right Cessation
- 1988-12-05 DK DK678188A patent/DK175463B1/en not_active IP Right Cessation
- 1988-12-20 CH CH4702/88A patent/CH675667A5/de not_active IP Right Cessation
- 1988-12-27 IT IT68157/88A patent/IT1224035B/en active
- 1988-12-28 AR AR88312869A patent/AR241624A1/en active
-
1989
- 1989-01-13 FR FR8900364A patent/FR2626143B1/en not_active Expired - Lifetime
- 1989-01-24 NL NL8900171A patent/NL188202C/en not_active IP Right Cessation
- 1989-01-25 IE IE22289A patent/IE62885B1/en not_active IP Right Cessation
- 1989-01-26 JP JP1015194A patent/JPH01215238A/en active Granted
- 1989-01-26 BR BR898900326A patent/BR8900326A/en not_active IP Right Cessation
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS63252560A (en) * | 1987-03-19 | 1988-10-19 | アルフア−ラヴアル セパレーシヨン アーベー | Centrifugal separator |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013504335A (en) * | 2009-09-16 | 2013-02-07 | ジーイーエー メカニカル エクイップメント ゲーエムベーハー | Method for producing raw milk that can be stored for a relatively long period of time |
WO2013069546A1 (en) * | 2011-11-07 | 2013-05-16 | テトラ ラバル ホールディングス アンド ファイナンス エス エイ | Method for producing and device for producing cheese starting material milk |
WO2013069547A1 (en) * | 2011-11-07 | 2013-05-16 | テトラ ラバル ホールディングス アンド ファイナンス エス エイ | Method for producing and device for producing starting material milk for skim milk |
CN103917089A (en) * | 2011-11-07 | 2014-07-09 | 利乐拉瓦尔集团及财务有限公司 | Method for producing and device for producing starting material milk for skim milk |
CN103917088A (en) * | 2011-11-07 | 2014-07-09 | 利乐拉瓦尔集团及财务有限公司 | Method for producing and device for producing cheese starting material milk |
Also Published As
Publication number | Publication date |
---|---|
AR241624A1 (en) | 1992-10-30 |
DK175463B1 (en) | 2004-11-01 |
AT396049B (en) | 1993-05-25 |
IE890222L (en) | 1989-07-27 |
CH675667A5 (en) | 1990-10-31 |
JPH0412933B2 (en) | 1992-03-06 |
NL8900171A (en) | 1989-08-16 |
DE3802305C1 (en) | 1989-10-05 |
IT1224035B (en) | 1990-09-26 |
DK678188A (en) | 1989-07-28 |
DK678188D0 (en) | 1988-12-05 |
BR8900326A (en) | 1989-09-19 |
IT8868157A0 (en) | 1988-12-27 |
NL188202B (en) | 1991-12-02 |
ATA290488A (en) | 1992-10-15 |
IE62885B1 (en) | 1995-03-08 |
FR2626143B1 (en) | 1992-12-31 |
NL188202C (en) | 1994-05-16 |
FR2626143A1 (en) | 1989-07-28 |
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