WO2018141055A1 - Method for consolidating mature fines tailings - Google Patents
Method for consolidating mature fines tailings Download PDFInfo
- Publication number
- WO2018141055A1 WO2018141055A1 PCT/CA2018/050106 CA2018050106W WO2018141055A1 WO 2018141055 A1 WO2018141055 A1 WO 2018141055A1 CA 2018050106 W CA2018050106 W CA 2018050106W WO 2018141055 A1 WO2018141055 A1 WO 2018141055A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- mft
- layer
- fluid
- tailings
- mature fines
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/02—General arrangement of separating plant, e.g. flow sheets specially adapted for oil-sand, oil-chalk, oil-shales, ozokerite, bitumen, or the like
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B1/00—Conditioning for facilitating separation by altering physical properties of the matter to be treated
- B03B1/04—Conditioning for facilitating separation by altering physical properties of the matter to be treated by additives
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
- C02F11/14—Treatment of sludge; Devices therefor by de-watering, drying or thickening with addition of chemical agents
- C02F11/148—Combined use of inorganic and organic substances, being added in the same treatment step
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
- C10G1/04—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction
- C10G1/045—Separation of insoluble materials
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
Definitions
- the present invention relates to treatment of tailings including mature fines tailings.
- tailings ponds arising from oil sands operations consist of three layers.
- the bottommost layer consists mostly of sand and large particles (>0.5 mm) that fall to the base of the pond under the action of gravity.
- the middle layer consists of mature fines tailings ("MFT"), a material that has the general consistency of yogurt and which contains a large amount of water and some residual oil trapped within the interstitial space of clays and fine sand.
- MFT mature fines tailings
- the topmost layer consists of mostly water with very fine solids suspended within the water.
- MFT is a composite material comprising water, clay, sand, and residual hydrocarbons.
- tailings including MFT are produced during the oil sands extraction process wherein the clay and solids are separated from the oil sand to yield bitumen.
- the tailings including MFT in typical practice, are deposited into large ponds where the sand component settles to the bottom of the system whereas the next densest material, the MFT, accumulates in a middle layer above the sand layer and below the water layer.
- the water can contain fine suspended particles that remain in suspension for considerable periods of time.
- the tailings materials that enter the tailings pond from the oil sands mining processing plant also contain oil. In typical practice, up to 1% of the material that is placed in the tailings pond is oil. However, this oil remains locked within the tailings material in the pond and is not produced from the pond.
- consolidation of MFT is achieved by using injection of a first fluid directly into the MFT layer, the fluid consisting of additives that help to achieve consolidation of the MFT.
- a second fluid is injected into the MFT to unlock the oil within the MFT. This oil can then be collected at the surface of the MFT for sale.
- a method for treating a mature fines tailings layer in a tailings deposit comprising the steps of: a. providing an injection system configured for injection of a first fluid, the first fluid comprising an additive effective to increase consolidation of the mature fines tailings layer; b. positioning the injection system so as to deliver the first fluid directly into the mature fines tailings layer; c. injecting the first fluid directly into the mature fines tailings layer; d. ceasing injection of the first fluid and allowing the first fluid and the additive to interact with the mature fines tailings layer; and e. allowing the mature fines tailings to further consolidate.
- the injection system comprises a well, which may be vertical, horizontal, deviated or multilateral.
- the injection system may alternatively comprise a distribution plate system, which may be a perforated plate system positioned at a base of the mature fines tailings layer or in an underlying sand layer or positioned near a top of the mature fines tailings layer.
- the additive in the first fluid preferably comprises at least one metal halide, which is preferably selected from the group consisting of aluminum chloride and iron chloride.
- a gas is directly injected into the mature fines tailings layer before or after the step of injecting the first fluid, and the gas is allowed to disturb the mature fines tailings layer and release entrapped hydrocarbon, and allowing the released hydrocarbon to rise to surface for collection.
- the gas is preferably selected from the group consisting of air, nitrogen, carbon dioxide, and mixtures thereof.
- the gas is most preferably carbon dioxide, and in such case exemplary methods may further comprise injecting a second fluid comprising an alkaline solution, and allowing the alkaline solution to interact with the carbon dioxide to produce carbonate to further consolidate and strengthen the mature fines tailings layer.
- a second fluid may be injected which comprises an additive selected from the group consisting of polymer and nanocrystals.
- the polymer is polyacrylamide and the nanocrystals are a cellulose nanocrystal suspension.
- One key advantage of the present invention is that the solids do not have to be mobilized for processing, e.g., transported to a barge, which means that the energy savings and thus cost savings for the present invention may be greater than that of conventional processes where the MFT is moved for processing.
- One novel aspect of the present invention lies in the use of wells or distribution systems to directly inject fluids into the reservoir to consolidate the MFT, and for the injection of additional fluids to yield oil from the MFT, and the collection of the oil from the system for sale.
- the present specification describes methods to consolidate MFT to a fraction of its present volume by direct injection of a set of water-borne chemicals into the MFT layer in the tailings pond. Furthermore, in some embodiments of the present invention a different set of fluids are optionally injected into the MFT layer to enhance mixing of the chemicals but to also mobilize trapped oil from the MFT to the top surface of the pond.
- MX aluminum, iron, sodium, potassium or copper
- X fluoride, chloride, bromide or iodide
- the mixture may be injected through a well (horizontal, vertical, deviated or multilateral) into the volume of MFT preferably such that the contact of the solution with the MFT is maximized.
- the well can also take the form of a distribution plate in some embodiments.
- gas is also injected into the MFT layer, preferably but not necessarily using the same well, to cause mixing of the solution and the MFT.
- the gas rises through the MFT causing movement and disturbance of the MFT and solution thus enabling the two to mix.
- the mixing could be done in alternate manners where, for example, the original solution is jetted into the MFT to achieve the mixing.
- the MFT consolidation is enhanced, and with the optional gas injection step some of the oil within the MFT is floated to the top of the water column above the MFT layer. This oil can be collected by skimming the pond.
- a cellulose nanocrystal suspension or polymer can be injected into the MFT, either before or after the gas injection step, to further consolidate the MFT.
- Polymers and nanocrystals and nanoparticles and microparticles can be added to either or both of the initial injected fluid and the gas.
- the nanoparticles/microparticles can consist of, for example, silica or iron oxide particles with or without functional acid/base groups and salts.
- the gas injected can consist of air, carbon dioxide, nitrogen, natural gas, or mixtures thereof.
- the method comprises: a. Drilling or placing a well or distribution system into the MFT layer of the tailings pond.
- the well is preferably completed using any existing completion technology that promotes uniform injectivity of the solution into the MFT layer, and the preferred embodiment is a horizontal well that sits a few meters above the base of the MFT layer, depending on the layer thickness.
- the volume of the primary solution injected should be large enough to contact the desired volume of MFT (the preferred embodiment is that at least 1 pore volume of primary solution is injected into the targeted volume of the MFT layer).
- the pore volume is defined as the volume in the MFT that is not solid - it is the volume of the fluids (water and oil) that is in the MFT .
- gas preferably nitrogen, carbon dioxide, air or a mixture of these components
- the gas rises through the MFT and mixes the solution and MFT by buoyancy forces.
- the gas injection step does not need to be long in duration but should be sufficient to sufficiently mix the system (the preferred embodiment is injection of greater than 1 pore volume of the targeted MFT layer).
- the system is left to sit and consolidate.
- a secondary solution containing alkaline materials can be injected into the MFT layer. This will react with the injected carbon dioxide to form carbonates which will further consolidate and strengthen the MFT layer.
- the carbon dioxide can be sourced from flue gas or upgrader process streams.
- the injection of the alkaline solution can be done directly after the primary solution or together with the primary solution.
- other materials such as polymers or cellulose nanocrystal can be injected into the MFT layer, as described above. h. Next, the oil that has floated to the top of the topmost water layer is collected by standard methods to collect oil slicks from the top of water layers.
- gas injection is not undertaken so as to only consolidate the MFT layer.
- gas injection may be done prior to the injection of the primary solution (Step b. above) to first release oil from the MFT. Thereafter, the primary solution is injected into the oil-depleted MFT layer.
- the present invention can also be used with non-oil sands tailings ponds such as mineral mining tailings ponds.
- non-oil sands tailings ponds such as mineral mining tailings ponds.
- FIG. 1A-H are diagrams exemplifying one implementation of the methods described herein for treating a MFT layer.
- FIG. 2A-B display results of using the method described here.
- FIG. 3 shows an example of the resulting MFT after the method described here is applied and the top water is removed.
- FIG. 4 shows an additional example of results for mixtures of additives with MFT.
- FIG. 5 shows an additional example of results after an exemplary method according to the present invention described herein is applied.
- FIG. 6 shows an additional example of results after an exemplary method according to the present invention described herein is applied.
- the present invention takes a new approach, and instead of moving the MFT to a surface facility for treatment, it is treated in situ within the pond and consolidates in place to allow reclamation.
- FIG. 1A-H illustrates an exemplary implementation of the present invention for consolidation of MFT with residual oil production.
- the original state of the tailings pond is displayed in FIG. 1 A.
- a well or distribution system is placed within the tailings layer, preferably within the base section of the MFT layer as shown in FIG. IB.
- MX aluminum, iron, sodium, potassium or copper
- X fluoride, chloride, bromide or iodide
- the pH can be altered to make the injected primary solution alkaline to enhance consolidation of the MFT layer.
- the most preferred materials in the primary solution are aluminum chloride and iron chloride.
- FIG. 1C displays the preparation of the primary solution on surface. This can also be done on a barge floating on the surface of the tailings pond or offsite.
- FIG. ID shows the step of injecting the primary solution into the MFT layer.
- the targeted volume of primary solution is preferably equal to at least one-half pore volume in the MFT layer.
- the preferred volume of primary solution is equal to 1 to 2 pore volumes of primary solution injected into the MFT layer.
- One-half pore volume of primary solution will be enough to achieve the desired effect, but it is preferable to have 1 to 2 pore volumes of primary solution.
- the greater the volume of primary solution the greater the reduction of electrostatic charges in the MFT.
- the MFT materials will react with the injectants and reduce the static electrical charges within the MFT and allow it to consolidate and release water. Also, in this step a small amount of oil will be released from the MFT materials.
- FIG. IE displays a 'soak' step where the primary solution is allowed to mix with the MFT layer. In this step the MFT will continue to react with the primary solution and some oil will be further released from the MFT.
- FIG. IF shows the next step of the process where a gas is injected into the MFT layer.
- the gas further mixes the MFT with the primary solution and also adheres to the released oil and due to buoyancy forces lifts the oil from the MFT layer to the top of the water layer above the MFT layer.
- the oil that is raised to the top of the water layer may be collected by skimming it from the top surface of the water.
- the preferred gas for this step is carbon dioxide, nitrogen, air or mixtures thereof.
- the amount of gas injected is preferably between one-half and three pore volumes (of the MFT layer) of gas. The preferred amount is 1-2 pore volumes of the MFT layer of gas.
- FIG. 1G illustrates another resting period after the gas has risen out of the MFT layer, showing the further-consolidated MFT.
- FIG. 1H a final step is shown, where if carbon dioxide was injected into the MFT layer in Step f, a secondary solution containing an alkaline base is added to the MFT to further consolidate the layer by having the carbon dioxide react with the alkaline solution to convert it to carbonates. This further consolidates the MFT layer and also strengthens it for future reclamation of the tailings pond.
- the alkaline solution can be, for example, calcium hydroxide or magnesium hydroxide with solutions of silicates or metal halides.
- the preferred components are calcium hydroxide and/or magnesium hydroxide.
- polymer or cellulose nanocrystals are added in the last injection step to further consolidate and strengthen the MFT.
- FIG. 2A-B shows an example of the results from using the method described here.
- FIG. 2A displays an example of the original MFT material.
- FIG. 2B shows two examples of the results of the consolidation and oil extraction procedure described herein. The results show that the water is rejected from the MFT layer and the MFT solids are consolidated.
- FIG. 3 shows the results of the MFT after gas injection and top water removal.
- the MFT is consolidated to about 50% of its original volume.
- the MFT layer was consolidated to between 15 and 50% of its original volume depending on the materials used and the gas injection volume.
- the MFT was consolidated to about 50% of its original volume and about 0.6 g of oil were extracted per 100 mL of MFT processed.
- the injection system can be located either on land or on a barge. Extended reach wells can be used if done from land.
- FIG. 4 shows the results of tests wherein a mixture of iron(III) chloride and polyacrylamide polymer was mixed with MFT (approximately 0.5 gallons) placed within a 2.5 gallon fish tank. Before the mixture was added to the tank, the MFT was either mixed with the iron(III) chloride and polyacrylamide polymer at either 1,000 or 20,000 rpm. The results display the amount of water spontaneously released from the MFT. In the case where water alone was added to the MFT, no water was released from the tailings mixture.
- MFT approximately 0.5 gallons
- FIG. 5 compares the final solid content of the Experiments A to E (pre-mix tests in 2.5 gallon tanks) to Experiment F (in-situ test in 2.5 gallon tank demonstrating the method described herein).
- Experiment F measurements of solids content were taken on the tailings samples treated by the in-situ method at the side of the tank where treatment solution and air were pumped into the tank from the sparger.
- FIG. 6 compares results of consolidation where different amounts of iron(III) chloride and polyacrylamide polymer are injected into a layer of MFT in a 2.5 gallon fish tank by using the method described here.
- the rate of height decrease was faster initially before about Hour 284 than that beyond Hour 294. It is interesting to note that this is the same time at which the fractures began to develop in the MFT due to the drying of the MFT.
- the opening of fractures in the deposits still produces a reduction in the volume of the tailings, however, this manifests as a shrinkage also in the lateral area of the tailings as the widths of the fractures extend laterally as well as vertically into the tailings volume.
- connection or coupling means any connection or coupling, either direct or indirect, between two or more elements; the coupling or connection between the elements can be physical, logical, or a combination thereof.
- a component e.g., a circuit, module, assembly, device, drill string component, drill rig system, etc.
- reference to that component should be interpreted as including as equivalents of that component any component which performs the function of the described component (i.e., that is functionally equivalent), including components which are not structurally equivalent to the disclosed structure which performs the function in the illustrated exemplary embodiments of the invention.
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Abstract
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Priority Applications (1)
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CA3066803A CA3066803C (en) | 2017-02-01 | 2018-01-30 | Method for consolidating mature fines tailings |
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US201762453030P | 2017-02-01 | 2017-02-01 | |
US62/453,030 | 2017-02-01 |
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Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120175315A1 (en) * | 2009-09-15 | 2012-07-12 | Suncor Energy Inc. | Process for Flocculating and Dewatering Oil Sand Mature Fine Tailings |
US20130206702A1 (en) * | 2012-02-15 | 2013-08-15 | Christopher Lin | Fluid tailings flocculation and dewatering using chemically-induced micro-agglomerates |
CA2932810A1 (en) * | 2012-06-21 | 2013-12-21 | Suncor Energy Inc. | Techniques for deposition and dewatering of thick fine tailings |
US8721896B2 (en) * | 2012-01-25 | 2014-05-13 | Sortwell & Co. | Method for dispersing and aggregating components of mineral slurries and low molecular weight multivalent polymers for mineral aggregation |
US20160089706A1 (en) * | 2014-09-30 | 2016-03-31 | SYNCRUDE CANADA LTD. in trust for the owners of the Syncrude Project, as such owners exist now and | Containment process for oil sands tailings |
CA2924305A1 (en) * | 2016-03-15 | 2017-09-15 | Syncrude Canada Ltd. | In-situ treatment of tailings |
-
2018
- 2018-01-30 WO PCT/CA2018/050106 patent/WO2018141055A1/en active Application Filing
- 2018-01-30 CA CA3066803A patent/CA3066803C/en active Active
- 2018-01-30 CA CA3189213A patent/CA3189213A1/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20120175315A1 (en) * | 2009-09-15 | 2012-07-12 | Suncor Energy Inc. | Process for Flocculating and Dewatering Oil Sand Mature Fine Tailings |
US8721896B2 (en) * | 2012-01-25 | 2014-05-13 | Sortwell & Co. | Method for dispersing and aggregating components of mineral slurries and low molecular weight multivalent polymers for mineral aggregation |
US20130206702A1 (en) * | 2012-02-15 | 2013-08-15 | Christopher Lin | Fluid tailings flocculation and dewatering using chemically-induced micro-agglomerates |
CA2932810A1 (en) * | 2012-06-21 | 2013-12-21 | Suncor Energy Inc. | Techniques for deposition and dewatering of thick fine tailings |
US20160089706A1 (en) * | 2014-09-30 | 2016-03-31 | SYNCRUDE CANADA LTD. in trust for the owners of the Syncrude Project, as such owners exist now and | Containment process for oil sands tailings |
CA2924305A1 (en) * | 2016-03-15 | 2017-09-15 | Syncrude Canada Ltd. | In-situ treatment of tailings |
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Publication number | Publication date |
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CA3066803C (en) | 2023-10-31 |
CA3189213A1 (en) | 2018-08-09 |
CA3066803A1 (en) | 2018-08-09 |
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