EP2293857A1 - Procede de traitement d'effluents liquides charges en hydrocarbures - Google Patents
Procede de traitement d'effluents liquides charges en hydrocarburesInfo
- Publication number
- EP2293857A1 EP2293857A1 EP08805619A EP08805619A EP2293857A1 EP 2293857 A1 EP2293857 A1 EP 2293857A1 EP 08805619 A EP08805619 A EP 08805619A EP 08805619 A EP08805619 A EP 08805619A EP 2293857 A1 EP2293857 A1 EP 2293857A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- treatment
- hydrocarbons
- treatment tank
- effluents
- reversible sorbent
- 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- Withdrawn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
Classifications
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
- C02F1/285—Treatment of water, waste water, or sewage by sorption using synthetic organic sorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D15/00—Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/0202—Separation of non-miscible liquids by ab- or adsorption
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/22—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
- B01J20/26—Synthetic macromolecular compounds
- B01J20/261—Synthetic macromolecular compounds obtained by reactions only involving carbon to carbon unsaturated bonds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/28—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties
- B01J20/28014—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof characterised by their form or physical properties characterised by their form
- B01J20/28042—Shaped bodies; Monolithic structures
- B01J20/28045—Honeycomb or cellular structures; Solid foams or sponges
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3425—Regenerating or reactivating of sorbents or filter aids comprising organic materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/345—Regenerating or reactivating using a particular desorbing compound or mixture
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/30—Processes for preparing, regenerating, or reactivating
- B01J20/34—Regenerating or reactivating
- B01J20/3483—Regenerating or reactivating by thermal treatment not covered by groups B01J20/3441 - B01J20/3475, e.g. by heating or cooling
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/008—Control or steering systems not provided for elsewhere in subclass C02F
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/02—Treatment of water, waste water, or sewage by heating
- C02F1/04—Treatment of water, waste water, or sewage by heating by distillation or evaporation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/26—Treatment of water, waste water, or sewage by extraction
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/28—Treatment of water, waste water, or sewage by sorption
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/16—Regeneration of sorbents, filters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2303/00—Specific treatment goals
- C02F2303/26—Reducing the size of particles, liquid droplets or bubbles, e.g. by crushing, grinding, spraying, creation of microbubbles or nanobubbles
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F9/00—Multistage treatment of water, waste water or sewage
Definitions
- the present invention relates to the general technical field of the treatment of effluents loaded with hydrocarbons.
- effluents loaded with hydrocarbons are for example industrial effluents of the kind of industrial process water, separator water, lagoon water or groundwater.
- Effluents can also come from refineries, oil extraction sites, oil tanker maintenance sites at ports or from industrial and chemical sites.
- the object of the present invention is to propose a new process for the treatment of effluents loaded with hydrocarbons, making it possible to overcome the drawbacks mentioned above and using a neutral and recyclable product.
- Another object of the present invention is to provide a simple and reliable processing installation for implementing the aforementioned method.
- the treatment process consists of using the reversible sorbent agent separated from the hydrocarbons to reintroduce it into the treatment tank.
- the treatment process consists in introducing into the tank of treatment a specific amount of reversible sorbent agent composed at least partly of reversible sorbent agent already used in the course of treatment.
- the treatment process consists of continuously monitoring the residual concentration of hydrocarbons in the effluents treated and extracted from the treatment tank to prevent any discharge of polluted water.
- the treatment method consists in determining, as a function of the residual concentration of hydrocarbons, whether the treated effluents are discharged or reintroduced into the treatment tank to undergo a cycle of complementary treatment.
- the treatment method consists in determining the hydrocarbon concentration of the liquid effluents introduced into the treatment tank and modulating the amount of reversible sorbent agent introduced into the treatment tank in accordance with the invention. of said concentration.
- the treatment process consists of determining the capacity of the reversible sorbent agent to fix the hydrocarbons before reuse.
- the treatment process consists in carrying out a desorption of the hydrocarbon-loaded reversible sorbent agent originating from the treatment tank, by using mechanical, thermal, chemical or biological means to using bacteria.
- the desorption operation may, if necessary, be completed with treatment with ultrasound, or by micro-bubbling or with treatment using a pulsating system.
- a mixer arranged in the treatment tank for mixing the liquid phase of the effluents and the solid phase of the reversible sorbent agent for fixing the hydrocarbons
- a means for conveying the reversible sorbent agent which binds the hydrocarbons to a mechanical, thermal, chemical or biological desorption system a means for conveying the reversible sorbent agent which binds the hydrocarbons to a mechanical, thermal, chemical or biological desorption system.
- a treatment tank for recovering the liquid effluents loaded with hydrocarbons, using a feed pipe opening into the treatment tank
- a feed system for the virgin or recycled reversible sorbent treatment tank said feed system injecting the reversible sorbent into the feed pipe
- This second treatment plant may be more efficient than the first in some cases of hydrocarbon composition and concentration.
- the objects assigned to the present invention are also achieved by means of a liquid effluent treatment system loaded with hydrocarbons, in particular to implement the treatment method presented above, said treatment system comprising a first installation as described above and a unit for pretreatment or post-treatment effluents respectively upstream or downstream of the first treatment facility, said preprocessing or post-treatment unit comprising a second installation of treatment as described above.
- composition and concentration of hydrocarbons in the effluents to be treated it may be necessary to use pre-treatment or post-treatment effluents to improve the effectiveness of treatment.
- the particular embodiments of the processing installation according to the invention and described hereinafter, may relate to the first and / or the second processing installation.
- the treatment plant comprises means for rerouting the reversible sorbent agent from the desorption system in the treatment tank.
- the treatment plant comprises an optional solvent addition system to the reversible sorbent agent fixing hydrocarbons and discharged from the treatment tank.
- the treatment plant comprises downstream of the hydrocarbon recovery means a distillation apparatus. evaporation to separate the solvent from the hydrocarbons, and a condensing apparatus for recovering the solvent in the liquid phase for reuse.
- the treatment plant comprises a means for controlling the hydrocarbon concentration of the effluents to be treated.
- the treatment plant comprises a means for controlling the residual hydrocarbon concentration of the effluents extracted in the lower part of the treatment tank.
- the treatment plant comprises means for controlling the capacity of the reversible reversible sorbent agent to fix hydrocarbons.
- the treatment plant comprises means for controlling the feed of the reversible sorbent treatment tank, as a function of the concentration of hydrocarbons in the effluents to be treated.
- the treatment tank is covered with two perforated walls and inclined so as to converge towards a substantially central position in which the screw-type evacuation means is arranged. transport, the effluent to be treated entering the treatment tank through the perforated walls.
- FIG. 1 illustrates an exemplary embodiment of a treatment installation according to the invention
- FIG. 2 illustrates a detail of the treatment tank of the treatment plant of FIG. 1 in a C-C direction view
- FIG. 3 illustrates a logic diagram relating to steps of an exemplary implementation of the treatment method according to the invention
- FIG. 4 illustrates another embodiment of a treatment installation according to the invention
- FIG. 5 schematically illustrates two embodiments of a processing system according to the invention, comprising a first and a second processing installation according to the invention.
- the treatment plant 11 in accordance with the invention and illustrated for example in FIG. 2, comprises a treatment tank 1 containing a reversible sorbent agent 2.
- This reversible sorbent agent 2 makes it possible to fix by surface effect the hydrocarbons with which it is in contact while being hydrophobic. Its reversibility makes it possible to desorb it a certain number of times and to reuse it in conditions close to those existing when it was virgin.
- the reversible sorbent agent 2 is preferably designed from a cellular plastics material of the polypropylene, polyethylene, polystyrene or any other material with similar characteristics, expanded and milled in the form of aggregates.
- the treatment tank 1 also contains liquid effluents 3 loaded with hydrocarbons 3b. The effluents 3 brought via a conduit 1a and are introduced into the treatment tank 1 from above, schematically according to the arrows A.
- a mixer 4 driven by a motor 5 is arranged in the treatment tank 1.
- the mixer 4 makes it possible to homogenize the diffusion of the reversible sorbent agent 2 in the effluents 3 to be treated.
- the installation comprises a gas or air injection system, called bubbling system, in the bottom of the treatment tank 1 to promote the separation of the liquid and solid phases in the treatment tank 1 and to improve the surface-binding properties of the reversible sorbant 2.
- a gas or air injection system called bubbling system
- the treatment plant also comprises a supply system 6 in virgin reversible sorbent agent 2.
- the feed system 6 comprises a reservoir 7 containing the reversible sorbent 2 and a transport screw 8 driven by a motor 9 for transporting and introducing said reversible sorbent agent 2 into the bottom of the treatment tank 1.
- the treatment plant also comprises a complementary feed system 10 made of recycled reversible sorbent agent 2.
- the complementary feed system 10 comprises a tank 1 1 containing the recycled reversible sorbent agent 2 and a transport screw 12 driven by a motor 13 for transporting and introducing said recycled reversible sorbent agent 2 into the bottom of the treatment tank 1
- the reservoir 11 is fed with the reversible sorbent agent 2 having undergone at least one desorption after at least one passage in the treatment tank 1.
- the treatment plant according to the invention also comprises, on the one hand, means for discharging the hydrocarbon-loaded reversible sorbent agent 2 in the upper part of the treatment tank 1 and, on the other hand, a conveying means. said reversible sorbent agent 2 loaded to a desorption system.
- the evacuation means and the conveying means are for example made using a transport screw 14 driven by a motor 15.
- the desorption system of the mechanical kind in the present example embodiment, comprises for example a compression screw 16 operating with a calibrated evacuation valve 17, moving against a restoring force of a tension spring 18 adjustable.
- the rotation of the compression screw 16 is for example ensured by the motor 15.
- the desorption system thus makes it possible to recover the liquid phase hydrocarbons 3b in a container 19 and the reversible sorbent agent 2 desorbed in solid phase in an additional container 20.
- the centrifugal mechanical desorption system comprises a mechanism for rotating the treatment vessel 1, which is mounted on a vertical or horizontal axis.
- the treatment tank 1 is then rotated when the decanted effluents have been extracted from said treatment tank 1.
- a second treatment tank 1 can then take over to ensure continuity in the treatment process according to the invention.
- the reversible sorbent 2 leaving the desorption system can be rerouted using adequate means in the tank 1 1, for reuse.
- the means of rerouting are materialized by the arrow S4.
- a means for extracting treated effluents 3a is provided in the lower part of the treatment tank. The extraction is shown by the arrow S1.
- the treatment plant further comprises a system for adding a solvent 21 from a reservoir of solvent 22.
- the solvent 21 is mixed with the hydrocarbon-laden reversible sorbent agent 2 of the conveying means upstream of the desorption system.
- the treatment plant also comprises a distillation-evaporation apparatus 23 for separating the solvent 21 from the hydrocarbons 3b, which are recovered in a hydrocarbon reservoir 24.
- the gas phase solvent (s) 21 are condensed in a condensation apparatus and conveyed into the solvent tank 22 by means of a pump 26 for reuse.
- the treatment tank 1 is covered with two perforated walls 27 and inclined so as to converge upwards towards a substantially central position above the treatment tank 1.
- One of the walls 27 advantageously delimits a housing 28 for the transport screw 14 and the compression screw 16.
- the treatment plant comprises a means for controlling the hydrocarbon concentration of the effluents 3 to be treated.
- the treatment plant also comprises a means for controlling the residual hydrocarbon concentration of the effluents extracted at the bottom of the treatment tank 1.
- the treatment plant according to the invention may also comprise means for controlling the capacity of the reversible reversible sorbent agent 2 to bind hydrocarbons. This control means ensures a minimum efficiency of the reversible sorbent agent 2, reused after one or more treatment cycles.
- This means of control of the desorbed reversible sorbent agent 2 can be a dimensional control, physical or other, for example a density control.
- the treatment plant comprises means for controlling the feed of the reversible sorbent treatment tank 2, for example as a function of the initial concentration of hydrocarbons in the effluents to be treated.
- control means managed for example by computer, make it possible to ensure optimal operation, continuously or in cycles, of the treatment installation according to the invention.
- a three-way valve 29 automatically controlled according to the residual hydrocarbon concentration in the treated effluents, makes it possible to select either a direct evacuation path to a sewerage network, shown schematically by the arrow S1, or a re-routing path to the treatment tank 1, shown schematically by the arrow S2.
- FIG. 3 illustrates various steps or phases of an exemplary implementation of the continuous treatment method according to the invention and this using a processing installation 11 (see FIG. 1) or FIG. Figure 4).
- the effluents 3 to be treated are conveyed into the treatment tank 1.
- the treatment tank 1 is fed with a reversible sorbent 2 having a determined particle size and according to step 300 the effluents 3 are mixed with the reversible sorbent 2 in the treatment tank 1 to charge said reversible sorbent agent 2 for fixing the hydrocarbons 3b contained in the effluents 3 on the reversible sorbant 2.
- the reversible sorbent agent 2 which binds the hydrocarbons accumulates, taking into account its density, in the upper part of the treatment tank 1. Then, according to step 400, the hydrocarbon-loaded reversible sorbent 2 is discharged from the treatment tank 1.
- the treated effluents 3a, purified hydrocarbons are then in the lower part of the treatment tank 1 and can be extracted, in step 500, from the lower portion of the treatment tank 1 said treated effluent 3a.
- step 600 the hydrocarbons 3b are separated from the charged reversible sorbent 2 from the treatment tank 1, by a mechanical desorption operation of the compression or centrifugation type or by any other operation referred to above.
- the recovered hydrocarbons 3b and the desorbed reversible sorbant 2 are then stored in steps 700 and 800, respectively.
- the treatment process consists of using the reversible sorbent agent 2 separated from the hydrocarbons 3b to reintroduce it into the treatment tank 1.
- the treatment process consists in introducing into the tank of treatment 1, a specific amount of reversible sorbent agent 2 composed at least partly of reversible sorbent agent 2 already used and desorbed at least once.
- the treatment method consists, according to a control step 550, in controlling the residual concentration of hydrocarbons 3b in the treated effluents 3a and extracted from the treatment tank 1.
- this residual concentration is below a determined threshold
- the treated effluents 3a are discharged with the wastewater, as indicated by the arrow S1.
- this residual concentration is still too great
- the treated effluents 3a are redirected to the treatment tank 1 in order to undergo an additional treatment cycle, as indicated with the arrow S2.
- the selection of the routing is either the arrow S1 or arrow S2 is preferably done automatically using a three-way valve 29, driven according to the residual concentration of hydrocarbons.
- the treatment process consists of determining the concentration of 3b hydrocarbons liquid effluents 3 introduced into the treatment tank 1 and modulating the amount of reversible sorbent agent 2 introduced into said tank of treatment 1, depending on said concentration.
- the treatment method consists, according to a control step 850, in determining the capacity of the reversible sorbent agent 2 to bind the hydrocarbons before reuse indicated by the arrow S4. Assuming that the quality of the desorbed reversible sorbent 2 is satisfactory, it is rerouted to the tank 1 1 hopper type. Otherwise, the reversible sorbent 2 is removed for thermal recovery or gasification, as indicated with the arrow S3.
- the treatment process consists of desorbing the hydrocarbon-loaded reversible sorbent 2 2b and taken from the treatment tank 1, having previously injected a solvent of so as to mix with said reversible sorbent agent 2 loaded so as to fluidize said hydrocarbons 3b and facilitate desorption. This is particularly suitable for recovering heavy 3b hydrocarbons. These are then mixed with the solvent.
- the treatment process then consists in recovering the solvent by evaporation followed by condensation in order to reuse it and not to reject it in the environment.
- the treatment method operates for example continuously or per cycle.
- a cycle corresponding to the filling of the treatment tank 1 with effluents 3 to be treated.
- the treatment plant according to the invention may be in traveling form so as to be able to move it to sites where it is necessary to treat effluents loaded with hydrocarbons.
- the treatment installation 12 in accordance with the invention comprises a supply pipe T in which the effluents to be treated flow forcefully along the arrow A.
- the feeding system 6 introduces the reversible sorbent agent 2 directly into the feed pipe T, which opens for example in the bottom of the treatment tank 1.
- a vortex-like 4v vortex generating means is inserted into the feed tubing T downstream of the injection point of the reversible sorbant 2.
- the vortex generating means 4v provides a better homogenization in the feed. dispersion of the reversible sorbent agent 2 in the liquid effluents to be treated.
- the flow rate in the feed pipe T is chosen so that the liquid effluents are able to overcome the Archimedes force of the reversible sorbent agent 2 injected into the feed pipe T and having a lower density than effluents.
- the length of the feed pipe T is chosen to ensure an optimal contact time between the reversible sorbent agent 2 and the effluents before their introduction into the treatment tank 1, preferably in a lower part.
- the reversible sorbent agent 2 then rises to the upper part of the treatment tank 1 by fixing hydrocarbons contained in the effluents.
- the effluents pass through a filter F before being extracted from the treatment tank 1, in the following ways schematized by the arrows S1 or S2 previously described in FIG.
- FIG. 5 schematically illustrates a system for treating liquid effluents charged with hydrocarbons, in particular for implementing the treatment method presented above, said treatment system comprising a first treatment plant 11 as described above. as well as a preprocessing or post-processing unit of effluents respectively upstream or downstream of the first treatment plant H 1 said pretreatment or post-treatment unit comprising a second processing installation 12 as described above.
- pre-treatment unit makes it possible to introduce the effluents to be treated E into the second treatment plant 12 before being taken out of the said second treatment plant 12 to be conveyed to the first treatment plant 11. The latter then rejects the ET treated effluents.
- a post-treatment unit makes it possible to introduce the effluents to be treated E into the first treatment plant 11 before being taken out of the said first treatment plant 11 to be conveyed to the second treatment plant. 12. The latter then rejects the ET treated effluents.
- the treatment method according to the invention has the advantage of recovering and reusing the functional components, namely reversible sorbant 2, solvent and water. In addition, no chemical or toxic products are released into the environment.
- the treated effluents 3a in general of the sanitized water, is eliminated by the sewerage network and the hydrocarbons 3b as well as the reversible sorbant 2 at the end of their life, are recovered thermally or gasified.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Analytical Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
Description
Claims
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PCT/FR2008/000729 WO2009144388A1 (fr) | 2008-05-28 | 2008-05-28 | Procede de traitement d'effluents liquides charges en hydrocarbures |
Publications (1)
Publication Number | Publication Date |
---|---|
EP2293857A1 true EP2293857A1 (fr) | 2011-03-16 |
Family
ID=40589843
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP08805619A Withdrawn EP2293857A1 (fr) | 2008-05-28 | 2008-05-28 | Procede de traitement d'effluents liquides charges en hydrocarbures |
Country Status (4)
Country | Link |
---|---|
US (1) | US8877050B2 (fr) |
EP (1) | EP2293857A1 (fr) |
CA (1) | CA2726017C (fr) |
WO (1) | WO2009144388A1 (fr) |
Families Citing this family (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2961405B1 (fr) * | 2010-06-18 | 2015-01-16 | Osead | Dispositif et procede pour la depollution de l'eau. |
WO2013162396A1 (fr) * | 2012-04-25 | 2013-10-31 | Siemens Aktiengesellschaft | Séparation d'une phase liquide à partir d'une émulsion |
JP6132630B2 (ja) * | 2013-04-02 | 2017-05-24 | 株式会社 アクセスジャパン | 油水混合物から油を分離するための油水分離装置および該装置を含む油水混合物から油を分離するための油水分離システム |
FR3006905B1 (fr) * | 2013-06-18 | 2015-06-26 | Osead Hydrocarbon Technologies | Dispositif pour extraire des hydrocarbures d'un melange liquide. |
IT201600085194A1 (it) * | 2016-08-12 | 2018-02-12 | Directa Plus Spa | Processo per il trattamento di acque contenenti idrocarburi mediante grafite espansa |
US10525415B2 (en) * | 2017-06-15 | 2020-01-07 | Saudi Arabian Oil Company | Processing systems for produced water and methods for recovering organic compounds from the produced water |
CN110180216B (zh) * | 2019-06-11 | 2021-05-25 | 南京农业大学 | 一种超声波强化流化床式树脂吸附-解析提取纯化花色苷的方法及装置 |
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FR2905702A1 (fr) * | 2006-09-11 | 2008-03-14 | Novad Soc Par Actions Simplifi | Procede et installation d'extraction d'huiles minerales |
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US2585491A (en) * | 1949-04-14 | 1952-02-12 | Sun Oil Co | Continuous adsorption process |
IL36739A0 (en) * | 1970-07-13 | 1971-06-23 | Hydronautics | Continuous fluid-solid contact method and apparatus |
US3798158A (en) * | 1971-05-26 | 1974-03-19 | Col Mont Corp | Process for removing oil and other organic contaminants from water |
US4279756A (en) * | 1976-05-03 | 1981-07-21 | Commonwealth Scientific And Industrial Research Organization | Water clarification |
US4461579A (en) * | 1981-07-31 | 1984-07-24 | Statiflo, Inc. | Motionless mixer combination |
US4478803A (en) * | 1983-02-07 | 1984-10-23 | The Hanna Mining Company | Dry scrubbing of SO2 from mixtures |
US4661256A (en) * | 1985-10-28 | 1987-04-28 | Uop Inc. | Process for the removal of hydrocarbonaceous compounds from an aqueous stream and hydrogenating these compounds |
US4752397A (en) * | 1986-06-30 | 1988-06-21 | Aluminum Company Of America | Process for removing heavy metal ions from solutions using adsorbents containing activated hydrotalcite |
US5135656A (en) * | 1989-12-15 | 1992-08-04 | Nalco Chemical Company | Process for removing water soluble organic compounds from produced water |
US5534153A (en) * | 1992-07-24 | 1996-07-09 | Martin Marietta Energy Systems, Inc. | Continuous fluidized-bed contactor with recycle of sorbent |
US5330636A (en) * | 1992-12-04 | 1994-07-19 | Adfiltech Corporation | Apparatus for continuous reconditioning of hydrocarbon fluids |
WO1994014513A1 (fr) | 1992-12-23 | 1994-07-07 | Union Oil Company Of California | Elimination d'hydrocarbures par extraction a contre-courant |
US6358422B1 (en) * | 1998-05-14 | 2002-03-19 | Amcol International Corporation | Method and apparatus for removing oil from water including monitoring of absorbent saturation |
US7445721B2 (en) * | 2003-12-03 | 2008-11-04 | Idaho Research Foundation, Inc. | Reactive filtration |
US7442293B2 (en) * | 2005-01-14 | 2008-10-28 | Jyonan Electric Industrial Corporation Limited | Oil/water separation apparatus for oil-containing mixture |
-
2008
- 2008-05-28 US US12/995,026 patent/US8877050B2/en not_active Expired - Fee Related
- 2008-05-28 WO PCT/FR2008/000729 patent/WO2009144388A1/fr active Application Filing
- 2008-05-28 EP EP08805619A patent/EP2293857A1/fr not_active Withdrawn
- 2008-05-28 CA CA2726017A patent/CA2726017C/fr not_active Expired - Fee Related
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
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US2614133A (en) * | 1949-06-30 | 1952-10-14 | Sun Oil Co | Continuous adsorption process |
FR2905702A1 (fr) * | 2006-09-11 | 2008-03-14 | Novad Soc Par Actions Simplifi | Procede et installation d'extraction d'huiles minerales |
Also Published As
Publication number | Publication date |
---|---|
WO2009144388A1 (fr) | 2009-12-03 |
US8877050B2 (en) | 2014-11-04 |
CA2726017A1 (fr) | 2009-12-03 |
CA2726017C (fr) | 2015-07-07 |
US20110076750A1 (en) | 2011-03-31 |
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