JPS6230515A - Apparatus for treating contaminated liquid - Google Patents
Apparatus for treating contaminated liquidInfo
- Publication number
- JPS6230515A JPS6230515A JP61143976A JP14397686A JPS6230515A JP S6230515 A JPS6230515 A JP S6230515A JP 61143976 A JP61143976 A JP 61143976A JP 14397686 A JP14397686 A JP 14397686A JP S6230515 A JPS6230515 A JP S6230515A
- Authority
- JP
- Japan
- Prior art keywords
- oil
- contaminants
- plastic
- separation
- chamber
- 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.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims description 13
- 239000000356 contaminant Substances 0.000 claims description 22
- 239000007787 solid Substances 0.000 claims description 16
- 229920001343 polytetrafluoroethylene Polymers 0.000 claims description 15
- 239000004810 polytetrafluoroethylene Substances 0.000 claims description 15
- 239000002245 particle Substances 0.000 claims description 11
- 239000004033 plastic Substances 0.000 claims description 6
- -1 polytetrafluoroethylene Polymers 0.000 claims description 4
- 239000011248 coating agent Substances 0.000 claims 1
- 238000000576 coating method Methods 0.000 claims 1
- 239000003921 oil Substances 0.000 description 24
- 238000000926 separation method Methods 0.000 description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 9
- 238000004140 cleaning Methods 0.000 description 4
- 230000000737 periodic effect Effects 0.000 description 3
- 239000002351 wastewater Substances 0.000 description 3
- 206010011878 Deafness Diseases 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000003763 carbonization Methods 0.000 description 2
- 239000000295 fuel oil Substances 0.000 description 2
- 239000010687 lubricating oil Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 101000606535 Homo sapiens Receptor-type tyrosine-protein phosphatase epsilon Proteins 0.000 description 1
- 102100039665 Receptor-type tyrosine-protein phosphatase epsilon Human genes 0.000 description 1
- 239000012790 adhesive layer Substances 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 239000008213 purified water Substances 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
- B01D21/0057—Settling tanks provided with contact surfaces, e.g. baffles, particles with counter-current flow direction of liquid and solid particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0003—Making of sedimentation devices, structural details thereof, e.g. prefabricated parts
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
- B01D21/0045—Plurality of essentially parallel plates
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
- B01D21/0069—Making of contact surfaces, structural details, materials therefor
- B01D21/0075—Contact surfaces having surface features
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/26—Separation of sediment aided by centrifugal force or centripetal force
- B01D21/262—Separation of sediment aided by centrifugal force or centripetal force by using a centrifuge
-
- 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
- B04B1/04—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls
- B04B1/08—Centrifuges with rotary bowls provided with solid jackets for separating predominantly liquid mixtures with or without solid particles with inserted separating walls of conical shape
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/08—Rotary bowls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B7/00—Elements of centrifuges
- B04B7/08—Rotary bowls
- B04B7/12—Inserts, e.g. armouring plates
- B04B7/14—Inserts, e.g. armouring plates for separating walls of conical shape
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
(産業上の利用分野)
本発明は液供給及び排出用接続部を存するとともに固体
粒子のデポジット形成汚染物を含む液を案内するガイド
面が設けられ、上記液を貫流させる少なくとも1つの処
理室を備える汚染液の処理装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial Field of Application) The present invention comprises liquid supply and discharge connections and is provided with a guide surface for guiding a liquid containing deposit-forming contaminants of solid particles, through which said liquid flows. The present invention relates to an apparatus for treating contaminated liquid, comprising at least one treatment chamber.
(従来の技術とその問題点)
上記した装置は、例えば燃料もしくは潤滑油用の固定式
もしくは遠心式の分離器、又は熱交換器等として使用で
きる。(Prior art and its problems) The above-described device can be used, for example, as a stationary or centrifugal separator for fuel or lubricating oil, or as a heat exchanger.
大型ディーゼルエンジンの燃料等として使用されるオイ
ルはモータに供給する前に水及び汚染物の除去を行わね
ばならない。通常これは遠心分離器により行われる。か
かる遠心分離器は同軸に配置された一群の円錐状の覆い
形弁離板を備え、これらの分離板は操作時に共通の中実
軸の回りで回転さ仕られる。上記中実軸の近傍に供給さ
れる、汚染されたオイルは一群の分離板を通して流れる
。Oil used as fuel in large diesel engines must be purified of water and contaminants before being supplied to the motor. Usually this is done using a centrifuge. Such a centrifugal separator comprises a group of coaxially arranged conical cover-shaped valve separation plates which, in operation, are rotated about a common solid axis. Contaminated oil supplied in the vicinity of the solid shaft flows through a group of separator plates.
オイル中の汚染物に作用する遠心力により、これらの汚
染物はオイルから確実に分離され、処理室の大径部に集
められる。浄化されたオイルは処理室の小径部から再度
排出される。The centrifugal force acting on the contaminants in the oil ensures that these contaminants are separated from the oil and collected in the large diameter section of the processing chamber. The purified oil is again discharged from the small diameter section of the processing chamber.
上記分離器がいわゆる自動排出タイプである場合、集め
られた汚染物は操作中の分離器から排出される。父上記
汚染物は分離器の分解後に除去することらできる。If the separator is of the so-called self-draining type, the collected contaminants are discharged from the separator during operation. The above contaminants can be removed after disassembly of the separator.
上記のような遠心分子s器及び他の装置において、液中
に存在する固体粒子が当該装置の処理室におけるガイド
面上にデポジットを形成するという問題が生じる。これ
により上記装置を定期的に分解して清掃する必要が生じ
、かかる作業を怠れば堆積した汚染物により上記装置に
閉塞が生じる。このように周期的に清掃を行わればなら
ず、それによりコスト高になるばかりでなく、上記装置
は汚染が増すにつれて操作が悪化する。清掃間隔を過度
に短くしないためには、上記装置に極めて太きな容量を
持たせねばならない。In centrifugal molecular analyzers and other devices such as those described above, a problem arises in that solid particles present in the liquid form deposits on the guide surfaces in the processing chamber of the device. This necessitates periodic disassembly and cleaning of the device; failure to do so may result in blockage of the device due to accumulated contaminants. Not only does this require periodic cleaning, which increases costs, but the equipment also deteriorates in operation as contamination increases. In order not to shorten the cleaning interval too much, the device must have a very large capacity.
(問題点を解決するための手段)
本発明は本明細書の発明の詳細な説明の欄の冒頭部分に
記載した種類の装置であって、しかも操作コストの低い
装置を提供することを目的とする。(Means for Solving the Problems) An object of the present invention is to provide a device of the type described at the beginning of the Detailed Description of the Invention column of this specification, which has a low operating cost. do.
本発明によれば、少なくとも汚染物のデポジットに最も
多くさらされる上記ガイド面における表面部をポリテト
ラフルオロエチレンの特性を有するプラスチックにより
形成することによって上述の目的が達成される。この結
果上記表面部にはもはやいかなる汚染物のデポジットら
存在せず、従って周期的な2回の清掃間の時間間隔をか
なり大幅に増加させうろことが判明した。According to the invention, the above object is achieved by forming at least the surface part of the guide surface which is most exposed to the deposits of contaminants from a plastic having the properties of polytetrafluoroethylene. It has been found that as a result of this, the surfaces are no longer free of any deposits of contaminants, thus increasing the time interval between two periodic cleanings considerably.
なべ等において非粘着層としてポリテトラフルオロエチ
レン(4フッ化エチレン樹脂:以下PTPEと略記する
)を使用することは従来から知られていた。PTFEは
特に過度に加熱した際の部分的な炭化による食物の付着
を防止する。本発明によればPTFEは堆積物の形成を
も防止しうろことが判明した。It has been known for a long time to use polytetrafluoroethylene (tetrafluoroethylene resin: hereinafter abbreviated as PTPE) as a non-adhesive layer in pans and the like. PTFE prevents food adhesion due to partial carbonization, especially when heated excessively. In accordance with the present invention, it has been found that PTFE may also prevent deposit formation.
この場合過熱の結果としての部分的な炭化による付着が
生じないのも疑問の余地がない。There is no doubt that in this case no adhesion occurs due to local carbonization as a result of overheating.
(実施例) 以下添付図面を参照しながら本発明の詳細な説明する。(Example) The present invention will be described in detail below with reference to the accompanying drawings.
第1図において、遠心分離器Iはハウジング2を備え、
該ハウジングは分離室3を包囲している。In FIG. 1, a centrifugal separator I comprises a housing 2,
The housing surrounds the separation chamber 3.
ハウジング2の周囲にケーシング(図示せず)が配置さ
れる。ハウジング2は軸5により回転駆動される。この
回転の結果分離室3内に遠心力場が形成され、この場内
で例えば固体粒子及び、ときには水により汚染されたオ
イルを浄化することができる。A casing (not shown) is arranged around the housing 2 . The housing 2 is rotationally driven by a shaft 5. As a result of this rotation, a centrifugal force field is created in the separation chamber 3 in which, for example, oil contaminated with solid particles and sometimes water can be purified.
汚染されたオイルは上記ケーシング中の適当な接続部材
を介して供給ライン4に供給される。この供給ライン4
の下端部に人口流路6が設けられ、該入口流路は分離車
3に連通している。The contaminated oil is fed into the supply line 4 via suitable connections in the casing. This supply line 4
An artificial flow path 6 is provided at the lower end of the inlet flow path, and the inlet flow path communicates with the separation wheel 3.
この分離室3内に多数の分離円板8が同軸に設けられて
いる。これらの円板8間に流路9が形成される。回転に
より形成される遠心力場により、(1(拾六λ1.f−
オイルの訪t1す去n才庁本右オX k!l l’i号
部分は外向きの力を加えられ、一方より軽量の構成部分
は内向きの力を加えられる。この結果固体粒子からなる
汚染物13は室3の最大径部に集まり、ときとして存在
する水も室3の最外周部に集まり、かつより軽量のオイ
ルは最小径部に集まる。A large number of separation disks 8 are provided coaxially within this separation chamber 3. A flow path 9 is formed between these disks 8 . Due to the centrifugal force field formed by rotation, (1(16λ1.f-
Oil's visit t1 left n-sai agency main office X k! The l l'i part is subjected to an outward force, while the lighter component is subjected to an inward force. As a result, contaminants 13 consisting of solid particles collect at the largest diameter of the chamber 3, water, sometimes present, also collects at the outermost periphery of the chamber 3, and the lighter oil collects at the smallest diameter.
上記オイル中の氷状要素部分は、室3の比較的大きな直
径部分で開始される流路15を介して上向きに流れ、通
路エツジ16に沿って水出口12に排出される。該水出
口は上記ケーシング内に形成される出口に公知の方法に
より接続される。The icy element fraction in the oil flows upwardly through a channel 15 starting in a relatively large diameter section of the chamber 3 and is discharged along a channel edge 16 to the water outlet 12 . The water outlet is connected to an outlet formed in the casing in a known manner.
通路エツジ16の半径を選択することにより、番号7に
より模式的に示す、分離室3内における水とオイルとの
分離レベルを調整できる。By selecting the radius of the passage edge 16, it is possible to adjust the level of separation of water and oil in the separation chamber 3, indicated schematically by number 7.
流路9内に存在するオイルはいまだ遠心力場の影響を受
け、いまだここに存在する汚染物はオイルから分離され
る。浄化されたオイルは排出路10を介してオイル出口
11に排出される。The oil present in the flow path 9 is still affected by the centrifugal field and any contaminants still present here are separated from the oil. The purified oil is discharged to an oil outlet 11 via a discharge passage 10.
図示の遠心分離51はいわゆる自動排出タイプである。The illustrated centrifugal separator 51 is of a so-called automatic discharge type.
このことは適当な方法によりハウジング下部をハウジン
グ上部に対し短い距離だけ移動させて2つのハウジング
部分間に汚染物排出用の流路を形成することにより、集
められた汚染物13を汚染物出口14を介して自動的に
排出しうろことを意味する。This can be accomplished by moving the lower part of the housing a short distance relative to the upper part of the housing by a suitable method to create a contaminant drainage channel between the two housing parts, thereby transferring the collected contaminants 13 to the contaminant outlet 14. This means that the scales will be automatically drained through.
ハウジングが分割されず、集められた汚染物を分解時に
周期的に除去するようにした具体例も知られている。Embodiments are also known in which the housing is not divided and the collected contaminants are periodically removed during disassembly.
本発明によれば、固体粒子を含む液が案内される表面部
がポリテトラフルオロエチレン(PTFE)又はそれと
同等の特性を有する材料により形成されている。第1図
において、このプラスチックが適用された部位をドツト
で示す。図示の如く室3の内壁はPTFE層18層上8
被覆されている。板8は完全にPTFEにより製造され
る。なお板8をステンレス鋼製とし、これらの板をPT
FEにより被覆しても良い。According to the invention, the surface portion through which the liquid containing solid particles is guided is formed of polytetrafluoroethylene (PTFE) or a material having properties equivalent to it. In FIG. 1, the areas to which this plastic is applied are indicated by dots. As shown in the figure, the inner wall of chamber 3 has 18 layers of PTFE.
Covered. Plate 8 is made entirely of PTFE. Note that the plate 8 is made of stainless steel, and these plates are made of PT.
It may be coated with FE.
本発明の一聾様によれば、分離板における力の場の力が
向けられる表面部のみにPTFEを備えることができる
。第1図の遠心分離器1において分離力は径方向外方に
向いており、このことは板の下面側をPTFE製とする
か、下面側をPTFEにより被覆できることを色味する
。これらの表面部は通常汚染物に最も多くさらされるの
で、まさに上記表面部をPTFEで製造することによっ
て最大の効果が得られる。According to one deaf aspect of the invention, only the surface portion of the separating plate on which the force of the force field is directed can be provided with PTFE. In the centrifugal separator 1 of FIG. 1, the separation force is radially outward, which suggests that the lower side of the plate can be made of PTFE or coated with PTFE. Since these surfaces are usually the most exposed to contaminants, the greatest benefit is obtained precisely by making these surfaces from PTFE.
第2図に示すように、本発明は固定式分離器25にも好
適に適用できる。この分離器25は主として水から固体
粒子及びオイルを除去することを意図するものである。As shown in FIG. 2, the present invention can also be suitably applied to a fixed separator 25. This separator 25 is primarily intended to remove solid particles and oil from water.
かかる分離器は例えば船上において汚水を浄化するのに
用いられる。Such separators are used, for example, on ships to purify waste water.
上記分離器25はハウジング26を備え、該ハウジング
内には分離室27が形成されている。汚水は汚水供給部
28を介して供給され、予備分離領域29に到着する。The separator 25 includes a housing 26 in which a separation chamber 27 is formed. The waste water is supplied via a waste water supply 28 and reaches a pre-separation area 29 .
汚染部分の分離が重力の作用により生じうるように全分
離器内における貫流速度は低く設定される。The flow rate in all separators is set low so that separation of the contaminated parts can occur under the influence of gravity.
オイルの一部は既に予備分離領域29の頂部に集められ
、このオイルはオイル出口34を介して排出させること
ができる。固体粒子汚染物の一部は上記予備分離領域内
で沈降して室27の底部上に横たわるようになる。A portion of the oil has already collected at the top of the pre-separation area 29 and this oil can be discharged via the oil outlet 34. Some of the solid particulate contaminants settle within the pre-separation zone and come to rest on the bottom of chamber 27.
その後予め浄化された水は一部の分離板30を介して低
い流速で上向きに流れる。これらの板30間に形成され
た流路内において、オイルの極めて微小な滴が融合して
大きな滴が形成される。このオイルは室27の頂部に集
められ、オイル出口32を介して排出させることができ
る。このようにしてオイル及び固体から浄化された水は
出口31から排出される。室27の底部に集められた固
体粒子は固体出口33を介して周期的に排出される。The pre-purified water then flows upwardly through some separation plates 30 at a low flow rate. Within the channels formed between these plates 30, extremely small droplets of oil coalesce to form larger droplets. This oil collects at the top of chamber 27 and can be drained via oil outlet 32. The water thus purified from oil and solids is discharged through outlet 31. The solid particles collected at the bottom of the chamber 27 are periodically discharged via the solids outlet 33.
本発明によれば、汚染物のデポジットにさらされた表面
部がPTFE又はそれと同等の特性を有する物質により
製造される。予備分離領域29の壁部及び処理室27の
底部はPTPEB35を備えている。固体粒子がこれら
の壁部と最も良く接触することを考慮すれば、デポジッ
トが形成される傾向はこれらの壁部において最も大きい
。又分離板30らPTFEで製造するか、もしくはl’
TFHにより被覆することができる。According to the invention, the surface area exposed to the deposit of contaminants is made of PTFE or a material with similar properties. The walls of the pre-separation area 29 and the bottom of the processing chamber 27 are provided with PTPEB 35. Considering that the solid particles are in the best contact with these walls, the tendency for deposits to form is greatest on these walls. Also, the separation plate 30 may be made of PTFE or l'
It can be coated with TFH.
本発明は分離?聾として使用するのがとりわけ好適であ
る。しかしこれらがデポジットを形成する固体粒子から
なる汚染物を含む液の処理全般を意図するものであるこ
とを考慮すれば、本発明は例えば燃料油予熱器又は潤滑
油冷却器等の熱交換器等にも、好ましい結果を伴って適
用できる。かかる熱交換器においては、流れ条件に応じ
て、固体粒子のデポジットが形成される傾向が生じうる
。Is the invention separate? It is particularly suitable for use as a deaf device. However, considering that these are intended for general treatment of liquids containing contaminants consisting of solid particles forming deposits, the present invention is applicable to heat exchangers such as fuel oil preheaters or lubricating oil coolers, etc. can also be applied with favorable results. In such heat exchangers, depending on the flow conditions, there can be a tendency for solid particle deposits to form.
これらのデポジットの形成は本発明の適用により効果的
に防止される。The formation of these deposits is effectively prevented by application of the present invention.
第1図は本発明に係る遠心分離器の縦断面図、第2図は
本発明に係る固定式分離器の垂直断面図である。
3.27・・・室、8.30・・・分離板、13・・汚
染物。
特許出願人 ユーロ・テクニカル・
オイルサービシズ・ビー、ブイ、FIG. 1 is a vertical cross-sectional view of a centrifugal separator according to the present invention, and FIG. 2 is a vertical cross-sectional view of a fixed separator according to the present invention. 3.27... Chamber, 8.30... Separation plate, 13... Contaminants. Patent applicant Euro Technical Oil Services B.V.
Claims (4)
子のデポジット形成汚染物を含む液を案内するガイド面
が設けられ、上記液を貫流させる少なくとも1つの処理
室を備える汚染液処理装置において、 上記汚染物のデポジットに最も多くさらされる上記ガイ
ド面における表面部を、ポリテトラフルオロエチレンの
特性を有するプラスチックにより形成したことを特徴と
する汚染液処理装置。(1) A contaminated liquid treatment device comprising at least one treatment chamber having liquid supply and discharge connections and provided with a guide surface for guiding a liquid containing solid particle deposit-forming contaminants, through which the liquid flows, A contaminated liquid treatment device characterized in that a surface portion of the guide surface that is most exposed to deposits of the contaminant is formed of a plastic having properties of polytetrafluoroethylene.
ある角度をなして配置される多数の分離板を有する分離
器とし、上記力の場における力の向けられる表面を上記
プラスチックにより形成した特許請求の範囲第1項に記
載の装置。(2) A patent in which the processing device is a separator having a number of separating plates arranged at a certain angle to the force field at least during operation, and the surface to which the force in the force field is directed is formed of the plastic. Apparatus according to claim 1.
した特許請求の範囲第1又は2項のいずれかに記載の装
置。(3) The device according to claim 1 or 2, wherein the plastic is applied as a surface coating.
た特許請求の範囲第2項に記載の装置。(4) The device according to claim 2, wherein the entire separating plate is made of the plastic.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
NL8501767A NL8501767A (en) | 1985-06-19 | 1985-06-19 | DEVICE FOR TREATING A POLLUTION-CONTAINING LIQUID. |
NL8501767 | 1985-06-19 |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6230515A true JPS6230515A (en) | 1987-02-09 |
Family
ID=19846167
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP61143976A Pending JPS6230515A (en) | 1985-06-19 | 1986-06-18 | Apparatus for treating contaminated liquid |
Country Status (5)
Country | Link |
---|---|
JP (1) | JPS6230515A (en) |
DE (1) | DE3619926A1 (en) |
ES (1) | ES296931Y (en) |
IT (1) | IT1189769B (en) |
NL (1) | NL8501767A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009514657A (en) * | 2003-07-10 | 2009-04-09 | ウエストファリア セパレーター アーゲー | Centrifuge with separation disk stack and separation disk |
JP2014533603A (en) * | 2011-11-28 | 2014-12-15 | アルファ・ラバル・コーポレイト・エービー | Centrifuge with anti-fouling properties |
JP2017537790A (en) * | 2014-12-10 | 2017-12-21 | ジー・イー・エイ メカニカル イクイプメント ゲゼルシャフト ミット ベシュレンクテル ハフツングGEA Mechanical Equipment GmbH | Separator |
Families Citing this family (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
SE504094C2 (en) * | 1995-03-06 | 1996-11-11 | Tetra Laval Holdings & Finance | Disc stack of centrifugal separator discs |
JP3573213B2 (en) | 1995-04-14 | 2004-10-06 | グラクソ、ウェルカム、インコーポレーテッド | Metered dose inhaler for beclomethasone dipropionate |
ES2206572T3 (en) | 1995-04-14 | 2004-05-16 | Smithkline Beecham Corporation | DOSE INHALER MEASURE FOR SALMETEROL. |
DE69622166T2 (en) | 1995-04-14 | 2003-04-03 | Smithkline Beecham Corp | DOSING INHALATOR FOR ALBUTEROL |
DE69636757T2 (en) | 1995-04-14 | 2007-10-11 | Smithkline Beecham Corp. | Dosing inhaler for fluticasone propionate |
DE10226695A1 (en) * | 2002-06-15 | 2003-12-24 | Daimler Chrysler Ag | Centrifugal oil separator in a crankcase of an internal combustion engine |
WO2012098055A1 (en) | 2011-01-17 | 2012-07-26 | F. Hoffmann-La Roche Ag | Separation apparatus and use thereof |
EP2859061B1 (en) * | 2012-05-30 | 2018-04-11 | NOV Process & Flow Technologies AS | System and method for removal of heavy metal ions from a rich hydrate inhibitor stream |
EP3207996B1 (en) | 2016-02-22 | 2019-05-08 | Alfa Laval Corporate AB | A centrifuge rotor for a centrifugal separator, a centrifugal separator, a method of separation, and a conical disk |
-
1985
- 1985-06-19 NL NL8501767A patent/NL8501767A/en not_active Application Discontinuation
-
1986
- 1986-06-13 DE DE19863619926 patent/DE3619926A1/en not_active Withdrawn
- 1986-06-18 JP JP61143976A patent/JPS6230515A/en active Pending
- 1986-06-18 IT IT12501/86A patent/IT1189769B/en active
- 1986-06-18 ES ES1986296931U patent/ES296931Y/en not_active Expired
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009514657A (en) * | 2003-07-10 | 2009-04-09 | ウエストファリア セパレーター アーゲー | Centrifuge with separation disk stack and separation disk |
JP4856540B2 (en) * | 2003-07-10 | 2012-01-18 | ウエストファリア セパレーター アーゲー | Centrifuge with separation disk laminate and separation disk |
JP2014533603A (en) * | 2011-11-28 | 2014-12-15 | アルファ・ラバル・コーポレイト・エービー | Centrifuge with anti-fouling properties |
JP2017537790A (en) * | 2014-12-10 | 2017-12-21 | ジー・イー・エイ メカニカル イクイプメント ゲゼルシャフト ミット ベシュレンクテル ハフツングGEA Mechanical Equipment GmbH | Separator |
Also Published As
Publication number | Publication date |
---|---|
ES296931U (en) | 1988-08-16 |
IT1189769B (en) | 1988-02-04 |
DE3619926A1 (en) | 1987-01-02 |
ES296931Y (en) | 1989-03-16 |
IT8612501A0 (en) | 1986-06-18 |
NL8501767A (en) | 1987-01-16 |
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