Classifications

• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
  • G01N30/02—Column chromatography
  • G01N30/50—Conditioning of the sorbent material or stationary liquid
  • G01N30/56—Packing methods or coating methods
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
  • B01F23/02—Maintaining the aggregation state of the mixed materials
  • B01F23/023—Preventing sedimentation, conglomeration or agglomeration of solid ingredients during or after mixing by maintaining mixed ingredients in movement
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
  • B01F23/60—Mixing solids with solids
  • B01F23/69—Mixing systems, i.e. flow charts or diagrams; Arrangements, e.g. comprising controlling means
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
  • B01F25/20—Jet mixers, i.e. mixers using high-speed fluid streams
  • B01F25/21—Jet mixers, i.e. mixers using high-speed fluid streams with submerged injectors, e.g. nozzles, for injecting high-pressure jets into a large volume or into mixing chambers
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
  • B01F25/50—Circulation mixers, e.g. wherein at least part of the mixture is discharged from and reintroduced into a receptacle
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
  • B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
  • B01F27/61—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis about an inclined axis
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
  • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
  • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
  • B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
  • B01F27/91—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with propellers
• • 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
• • 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
  • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
  • B01J8/005—Separating solid material from the gas/liquid stream
  • B01J8/007—Separating solid material from the gas/liquid stream by sedimentation
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
  • G01N30/02—Column chromatography
  • G01N30/50—Conditioning of the sorbent material or stationary liquid
• • 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
  • B01D15/08—Selective adsorption, e.g. chromatography
  • B01D15/10—Selective adsorption, e.g. chromatography characterised by constructional or operational features
  • B01D15/20—Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to the conditioning of the sorbent material
• • 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
  • B01D15/08—Selective adsorption, e.g. chromatography
  • B01D15/10—Selective adsorption, e.g. chromatography characterised by constructional or operational features
  • B01D15/20—Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to the conditioning of the sorbent material
  • B01D15/206—Packing or coating
• • G—PHYSICS
  • G01—MEASURING; TESTING
  • G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
  • G01N30/00—Investigating or analysing materials by separation into components using adsorption, absorption or similar phenomena or using ion-exchange, e.g. chromatography or field flow fractionation
  • G01N30/02—Column chromatography
  • G01N30/50—Conditioning of the sorbent material or stationary liquid
  • G01N30/56—Packing methods or coating methods
  • G01N2030/562—Packing methods or coating methods packing
  • G01N2030/565—Packing methods or coating methods packing slurry packing

Definitions

• the present invention relates to a method and a tank for suspending separation media slurry according to the preambles of claim 1, 3 and 7.
• Separation media could be for example chromatography media and density gradient media.
• the media could be for example resins based on natural or synthetic polymer particles or inorganic material.
• For chromatography the separation media needs to be provided into a chromatography column.
• the separation media is normally suspended with a liquid, for example water, buffer or a solvent. This suspended media is usually called media slurry.
• an intermediate tank is used where the slurry is mixed into a homogenous mixture.
• the media slurry is often stirred manually in the tank and it is important that the media slurry becomes a homogenous mixture regarding the distribution of different sizes of particles in the media.
• Another way to mix the slurry that is sometimes used is to shake or tilt the tank back and forth. This could be advantageous for small tanks and. small volumes of slurry but is hard to perform and not suitable for big, heavy tanks.
• An object of the present invention is to provide an improved method and tank for suspending separation media slurry before transportation of said media slurry into for example a column where particles in said media are not damaged.
• the impeller does not need to start in a thick, sedimented media with the risk of damaging particles in the media and the impeller does not need to be running the whole time when the separation media is inside the tank.
• the spraying of liquid by the nozzle starts the re-suspension of the media from the bottom of the tank and the impeller can be started when the media has been sufficiently re-suspended.
• liquid from the liquid phase of the media slurry having started to sediment is used for the spraying by the nozzle and hereby no new liquid need to be added and hereby the slurry concentration can be kept constant.
• Figure 1 is a schematic view of a separation media slurry tank according to the invention.
• Figure 2 is a flow chart describing the steps of the method.
• Figure 1 is a schematic view of a separation media slurry tank 1 according to the invention. If media is to be fed to a column from a media storage container the media is first transferred from the storage container to a media tank according to the invention.
• the media slurry can be pumped from the media storage container to the tank.
• the media could be transferred from the storage container to the tank using another pump and some other tubes or pipes.
• An impeller 7 that is provided inside the tank can be started from the beginning and keep on stirring the media slurry the whole time until the media has been transferred to a column where it should be used for, for example chromatography, but according to the invention, as will be further described below, the impeller does not need to be ongoing the whole time.
• the impeller 7 is preferably designed as a coil in the height direction of the tank, this kind of impeller is also called a helical ribbon. Other designs such as a two- or three- bladed propeller or an impeller formed as an anchor are however also possible. In Figure 1 a two-bladed propeller 7 is shown. Furthermore the impeller is suitably provided with its lowest end close to the bottom 8 of the tank.
• a nozzle 9 is furthermore provided protruding into the tank from the bottom 8 of the tank.
• This nozzle is connected to the pump 3, which in turn is connected to the adjustable pipe 5 as described above.
• the adjustable pipe 5 can be adjusted to have its open end 6 in a liquid phase provided above the sedimented media as soon as the media slurry is starting to sediment.
• the pump 3 pumps liquid from the liquid phase, through the adjustable pipe 5 and further to the nozzle 9.
• the pump applies a pressure to the liquid in the nozzle and the nozzle is designed such that the liquid is introduced with some speed, such as spraying, into the sedimented media from the bottom 8 of the tank. This has the advantage that the sedimented media in the tank will start to re-suspend.
• the impeller is not started until the sedimented media has been sufficiently re-suspended by the spraying from the nozzle.
• the impeller is easier to start the impeller than it would have been if the impeller would have to start inside thick, sedimented media and the risk for damaging particles of the media is minimized.
• the use of the liquid from the liquid phase of the sedimented media slurry for the spraying by the nozzle implies that no extra liquid need to be provided and the media slurry concentration can be kept constant.
• the tank according to the invention can also be used when transferring media from a column to a storage container. It could be suitable to first transfer the media to the tank, suspend the media sufficiently according to what was previously described and then transfer the media slurry to the storage container.
• Media slurry is first transferred from the storage container to the tank according to the invention. This could be done by using a pump and a tube or pipe. Possibly a pump 3 connected to the tank and the adjustable pipe 5 of the tank can be used for this transferring of media slurry from the storage container to the tank. As soon as the media slurry has entered the tank it starts to sediment — actually it is already sedimented to some degree since no stirring has been performed in the storage container, i.e. media will sediment at the bottom 8 of the tank and a liquid phase (possibly containing some particles also) will be built up over the sedimented media.
• the method steps S2-S11 need not to be performed immediately after transferring of the media slurry to the tank. But when it is time for the transferring of the media slurry to the column the media slurry needs to be mixed into an homogenous media slurry and then the steps S2-S11 will be performed.
• S3 The next step is to pump liquid from the liquid phase through the adjustable pipe 5 by using the pump 3.
• SI l When the media slurry is sufficiently mixed it is transferred to the column.

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Analytical Chemistry (AREA)
• General Health & Medical Sciences (AREA)
• Immunology (AREA)
• Health & Medical Sciences (AREA)
• Life Sciences & Earth Sciences (AREA)
• Biochemistry (AREA)
• Organic Chemistry (AREA)
• General Physics & Mathematics (AREA)
• Physics & Mathematics (AREA)
• Pathology (AREA)
• Structures Of Non-Positive Displacement Pumps (AREA)
• Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
• Mixers Of The Rotary Stirring Type (AREA)
• On-Site Construction Work That Accompanies The Preparation And Application Of Concrete (AREA)
• Separation Using Semi-Permeable Membranes (AREA)

Priority Applications (7)

Applications Claiming Priority (2)

Publications (1)

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Family Applications (1)

Country Status (8)

Cited By (2)

Families Citing this family (10)

Citations (3)

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• 2007
  • 2007-12-18 CN CN2007800491514A patent/CN101573614B/zh active Active
  • 2007-12-18 BR BRPI0719421A patent/BRPI0719421B8/pt active IP Right Grant
  • 2007-12-18 US US12/517,447 patent/US8092073B2/en active Active
  • 2007-12-18 DE DE602007014099T patent/DE602007014099D1/de active Active
  • 2007-12-18 EP EP07852125A patent/EP2100136B1/en active Active
  • 2007-12-18 WO PCT/SE2007/001125 patent/WO2008082339A1/en not_active Ceased
  • 2007-12-18 AT AT07852125T patent/ATE506612T1/de active
  • 2007-12-18 JP JP2009543982A patent/JP4975826B2/ja active Active

Patent Citations (3)

Non-Patent Citations (1)

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