FR3048621A1 - CONCENTRIC TRAP FOR SOLID PARTICLES IN LIQUIDS - Google Patents
CONCENTRIC TRAP FOR SOLID PARTICLES IN LIQUIDS Download PDFInfo
- Publication number
- FR3048621A1 FR3048621A1 FR1600397A FR1600397A FR3048621A1 FR 3048621 A1 FR3048621 A1 FR 3048621A1 FR 1600397 A FR1600397 A FR 1600397A FR 1600397 A FR1600397 A FR 1600397A FR 3048621 A1 FR3048621 A1 FR 3048621A1
- Authority
- FR
- France
- Prior art keywords
- filter
- solid particles
- liquids
- cylindrical shape
- trap
- 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.)
- Withdrawn
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 8
- 239000002245 particle Substances 0.000 title claims abstract description 7
- 239000007787 solid Substances 0.000 title claims abstract description 7
- 238000001914 filtration Methods 0.000 claims description 3
- 238000010926 purge Methods 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims 3
- 238000009434 installation Methods 0.000 abstract description 2
- 239000000571 coke Substances 0.000 description 5
- 230000002035 prolonged effect Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/11—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with bag, cage, hose, tube, sleeve or like filtering elements
- B01D29/31—Self-supporting filtering elements
- B01D29/35—Self-supporting filtering elements arranged for outward flow filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/88—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices
- B01D29/94—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor having feed or discharge devices for discharging the filter cake, e.g. chutes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2201/00—Details relating to filtering apparatus
- B01D2201/02—Filtering elements having a conical form
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
L'invention permet de filtrer les particules solides dans les liquides en limitant les pertes de charge. Le dispositif est constitué d'un panier maillé de forme conique sur sa partie supérieure (1) (fig 3) et de forme cylindrique sur sa partie inférieure (2)(fig 3) Les particules solides sont dirigées par la forme conique vers le centre du filtre et sont piégées concentriquement dans la forme cylindrique centrale tandis que les liquides s'écoulent librement sans perte de charge. Ce filtre peut fonctionner en continu grâce à un système de sassage (fig 4). Ce dispositif est préconisé sur les installations pétrolières.The invention makes it possible to filter the solid particles in the liquids by limiting the pressure drops. The device consists of a conical shaped mesh basket on its upper part (1) (FIG. 3) and of cylindrical shape on its lower part (2) (FIG. 3). The solid particles are directed by the conical shape toward the center of the filter and are trapped concentrically in the central cylindrical shape while the liquids flow freely without loss of load. This filter can operate continuously thanks to a system of sassage (fig 4). This device is recommended on oil installations.
Description
La présente invention concerne un dispositif pour filtrer les particules solides dans un liquide en limitant les pertes de charge pour assurer un débit constant de ce liquideThe present invention relates to a device for filtering solid particles in a liquid by limiting the pressure losses to ensure a constant flow rate of this liquid
Ce dispositif est préconisé dans le domaine du raffinage pétrolier. La filtration des hydrocarbures liquides est traditionnellement assurée soit par un filtre situé à l'aspiration d'une pompe (fig l)soit par un filtre de ligne (fig 2).De par leur design, les filtres se retrouvent rapidement obstrués par une petite quantité de matière solide ( type coke) ce qui occasionne de graves perturbations de l'installation .Les problèmes engendrés par ces perturbations sont : des cavitations de pompe causées par la perte de débit et de pression avec des risques de casse matériel et de feu .Cela se traduit par des pertes de production, des frais de maintenance et des dangers pour la sécurité des intervenants.This device is recommended in the field of petroleum refining. The filtration of liquid hydrocarbons is traditionally ensured either by a filter located at the suction of a pump (fig 1) or by a line filter (fig 2). By their design, the filters are quickly clogged by a small amount of solid material (coke type) which causes serious disturbances of the installation. The problems caused by these disturbances are: pump cavitations caused by the loss of flow and pressure with risks of material breakage and fire. This results in production losses, maintenance costs and safety hazards for the responders.
Dans le cas d'un filtre installé sur une pompe, ce filtre est un petit panier {fig 1 ) emmanché perpendiculairement dans la tuyauterie d'aspiration de la pompe .En marche perturbée {suite à un arrêt prolongé de l'unité ou suite à un pigging ) ce fiitre montre très rapidement ses limites et se retrouve vite bouché malgré une quantité de coke négligeable.In the case of a filter installed on a pump, this filter is a small basket {Fig. 1) fitted perpendicularly in the suction pipe of the pump. In disturbed operation {following a prolonged stoppage of the unit or following a pigging) this fiiter shows very quickly its limits and is quickly clogged despite a negligible amount of coke.
Dans le cas d'un filtre monté en ligne, ce panier est de plus grande dimension ( fig 2 ) mais le problème rencontré est que le peu de coke qui y entre vient se coller sur la grille côté aspiration de la pompe et l'obstrue assez rapidement. Le constat qui est fait en général au démontage de ce filtre est que selon la différence de pression entre l'entrée et la sortie du filtre, celui-ci semble remplit alors qu'il n'y a que très peu de coke à l'intérieur. L'innovation proposée est un piège concentrique afin de séparer les déchets solides dans les liquides (fig 3). En effet, lors des démarrages d'unités suite à un arrêt prolongé ou suite à un "pigging", nous sommes confrontés à un problème d'arrivée plus ou moins massive de particules solides comme le coke. Les filtres mis en place ne sont pas conçus pour contenir tous ces déchets aussi nous devons les nettoyer très souvent et une baisse de ia charge de l'unité est inévitable.In the case of a filter mounted in line, this basket is larger (Figure 2) but the problem is that the little coke that comes in sticks to the grid suction side of the pump and obstructs fast enough. The report that is generally made to disassembly of this filter is that according to the pressure difference between the inlet and the outlet of the filter, it appears to fill while there is very little coke in the filter. inside. The proposed innovation is a concentric trap to separate solid waste into liquids (Fig. 3). Indeed, when starting units after a prolonged shutdown or following a "pigging", we are faced with a problem of more or less massive arrival of solid particles such as coke. The filters put in place are not designed to contain all these wastes so we have to clean them very often and a drop in the load of the unit is inevitable.
Le design du piège concentrique est conçu pour canaliser les particules solides en son centre afin de laisser librement le débit se faire sur les côtés du filtre en limitant fortement les pertes de charge avec une possibilité de purge en continu via un système de sassage (fig 4) .Le but étant de limiter les manœuvres sur les filtres et les pompes et de ce fait capter au maximum les marges par un débit d'unité maxi et constant.The design of the concentric trap is designed to channel the solid particles at its center to freely let the flow be on the sides of the filter by greatly limiting the pressure drop with a possibility of continuous purge via a sassage system (fig 4 The goal is to limit the maneuvers on the filters and pumps and thus capture maximum margins by a maximum and constant unit flow rate.
Claims (2)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1600397A FR3048621A1 (en) | 2016-03-08 | 2016-03-08 | CONCENTRIC TRAP FOR SOLID PARTICLES IN LIQUIDS |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR1600397A FR3048621A1 (en) | 2016-03-08 | 2016-03-08 | CONCENTRIC TRAP FOR SOLID PARTICLES IN LIQUIDS |
Publications (1)
Publication Number | Publication Date |
---|---|
FR3048621A1 true FR3048621A1 (en) | 2017-09-15 |
Family
ID=56801583
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR1600397A Withdrawn FR3048621A1 (en) | 2016-03-08 | 2016-03-08 | CONCENTRIC TRAP FOR SOLID PARTICLES IN LIQUIDS |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR3048621A1 (en) |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4473470A (en) * | 1981-06-17 | 1984-09-25 | Boving & Co. (Anz.) Pty. Ltd. | Fluid strainer |
EP0596857A1 (en) * | 1992-11-06 | 1994-05-11 | Andritz-Patentverwaltungs-Gesellschaft m.b.H. | Process and device for separating mixtures of solids and liquids |
US5840180A (en) * | 1997-06-02 | 1998-11-24 | John Meunier Inc. | Water flow segregating unit with endless screw |
EP1043054A2 (en) * | 1999-03-31 | 2000-10-11 | Delphi Technologies, Inc. | Filter |
DE10049783A1 (en) * | 2000-10-09 | 2002-05-02 | Cremer Franz Wilhelm | Filter element for separation of solid foreign material from rain water in roof drainage system |
-
2016
- 2016-03-08 FR FR1600397A patent/FR3048621A1/en not_active Withdrawn
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4473470A (en) * | 1981-06-17 | 1984-09-25 | Boving & Co. (Anz.) Pty. Ltd. | Fluid strainer |
EP0596857A1 (en) * | 1992-11-06 | 1994-05-11 | Andritz-Patentverwaltungs-Gesellschaft m.b.H. | Process and device for separating mixtures of solids and liquids |
US5840180A (en) * | 1997-06-02 | 1998-11-24 | John Meunier Inc. | Water flow segregating unit with endless screw |
EP1043054A2 (en) * | 1999-03-31 | 2000-10-11 | Delphi Technologies, Inc. | Filter |
DE10049783A1 (en) * | 2000-10-09 | 2002-05-02 | Cremer Franz Wilhelm | Filter element for separation of solid foreign material from rain water in roof drainage system |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PLFP | Fee payment |
Year of fee payment: 2 |
|
PLSC | Publication of the preliminary search report |
Effective date: 20170915 |
|
PLFP | Fee payment |
Year of fee payment: 3 |
|
PLFP | Fee payment |
Year of fee payment: 4 |
|
ST | Notification of lapse |
Effective date: 20201110 |