TANGENTIAL FLOW FILTRATION APPARATUSES, SYSTEMS, AND PROCESSES FOR THE SEPARATION OF COMPOUNDS

• US 20140166555A1
• Filed: 08/08/2013
• Published: 06/19/2014
• Est. Priority Date: 03/31/2006
• Status: Abandoned Application

• Current Assignee: Danisco USA Incorporated (International Flavors & Fragrances Incorporated)
• Original Assignee: Danisco USA Incorporated (International Flavors & Fragrances Incorporated)
• Inventors: FONG, Robin, HENG, Meng H., DIBEL, Kevin R., ROZEBOOM, Glenn
• Application Number:
  US13/962,916
• Publication Number:
  US 20140166555A1
• Time in Patent Office: Days
• US Class Current: 210/87
• CPC Class Codes: B01D 2311/04 Specific process operations in the feed stream; Feed pretreatment
• CPC Class Codes: B01D 2311/16 Flow or flux control
• CPC Class Codes: B01D 2315/10 Cross-flow filtration
• CPC Class Codes: B01D 2315/16 Diafiltration
• CPC Class Codes: B01D 2317/022 Reject series
• CPC Class Codes: B01D 61/146 comprising multiple ultrafiltration steps
• CPC Class Codes: B01D 61/147 Microfiltration
• CPC Class Codes: B01D 61/1471 comprising multiple microfiltration steps
• CPC Class Codes: B01D 61/149 Multistep processes comprising different kinds of membrane processes selected from ultrafiltration or microfiltration
• CPC Class Codes: B01D 61/16 Feed pretreatment
• CPC Class Codes: B01D 61/18 Apparatus therefor
• CPC Class Codes: B01D 61/20 Accessories; Auxiliary operations
• CPC Class Codes: B01D 61/22 Controlling or regulating
• CPC Class Codes: C12M 47/10 Separation or concentration of fermentation products bioreactors combined with means for distillation or extraction of liquid fuel C12M43/02
• CPC Class Codes: C12M 47/12 Purification C12M47/04 takes precedence

Abstract

The invention relates to apparatuses, machines, systems and methods for the recovery and purification of proteins, peptides, nucleic acids, biologically produced polymers and other compounds from aqueous fluids. The aqueous fluids can comprise enzyme concentrates and or a fermentation broth with or without cells or other starting material. The fermentation broth can be produced by fermentations of fungal, yeast, bacterial, mammalian, insect or plant cells.

Claims

1-51. -51. (canceled)

52. A filtration system comprising a plurality of fluidly-interconnected filtration modules including a first module and multiple subsequent modules, wherein each module is configured to route received feed material and diluent adjacent a filter to provide permeate and retentate, the first module receiving feed at an inlet side from outside the system and the subsequent modules receiving retentate from a preceding module within the system as feed material, at least one of the modules having a permeate withdrawal flow line for withdrawing permeate from the system, and a plurality of the modules having a return permeate exit configured for feeding permeate back to an inlet side of a same or a preceding module within the system.

53. The system of claim 52, further comprising a control system configured for independent adjustment of one of product yield, product purity, net permeation rate, and overall flux while maintaining the three other variables approximately constant.

54. The system of claim 52, wherein the first and subsequent modules each have a permeate recycling line for returning permeate to the inlet side of the same module, and the modules subsequent to the first module further comprise a permeate recirculation line for backfeeding permeate to a preceding module within the system.

55. A filtration system comprising:

a system inlet for receiving fresh feed from outside the system,

a plurality of fluidly-interconnected filtration modules comprising a first module and multiple subsequent modules,

wherein the first module comprises;

an inlet side in fluid communication with the system inlet for receiving fresh feed, a diafiltration line for introducing diluent to the inlet side, a filter for selectively separating a species of interest from feed material comprising a mixture of fresh feed and diluent for providing permeate that passes through the filter to an outlet side of the module and retentate that does not pass through the filter, at least one permeate flow line for withdrawing permeate from the outlet side of the first module and optionally another permeate flow line for recycling permeate to the inlet side of the first module, and a retentate flow line configured to route retentate flow from the inlet side of the module to the inlet side of a subsequent module,

wherein the subsequent modules each comprise;

an inlet side in fluid communication with a retentate flow line of a preceding module, a diafiltration line for introducing diluent to the inlet side, a filter for selectively separating the species of interest from feed material introduced at the inlet side thereof, a permeate flow line configured for returning permeate flow from the outlet side of the module to the inlet side of the same module or for backfeeding permeate flow to a preceding module, another permeate flow line configured for withdrawing permeate from the system, and a retentate flow line configured to route retentate from the inlet side of the module to the inlet side of a subsequent module or otherwise discharge the retentate for recovery or recirculation within the system.

56. The system of claim 55, wherein the first and subsequent modules each have a permeate recycling line for returning permeate to the inlet side of the same module, and the modules subsequent to the first module further comprise a permeate recirculation line for backfeeding permeate to a preceding module within the system.

57. The system of claim 56, further comprising blending control for combining withdrawn permeate flows of two or more of the modules effective to provide a product having a targeted overall purity.

58. The system of claim 56, wherein the retentate flow line from each of the plurality of the modules is configured to route retentate from the retentate exit of a module to the inlet side of a next subsequent module.

59. The system of claim 56, wherein each filter comprises a membrane.

60. The system of claim 56, wherein the plurality of modules comprises 3 to 25 modules.

61. The system of claim 56, further comprising a control system to independently adjust one of product yield, product purity, net permeation rate, and overall flux while maintaining the three other variables approximately constant.

62. The system of claim 56, further comprising a plurality of pumps and valves for pumping and regulating flow of fluid through the system.

63. The system of claim 62, further comprising a plurality of sensors for acquiring data about fluid as it flows through the system, an electronic data processing network capable of at least receiving, transmitting, processing, and recording data associated with the operation of said pumps, valves, and sensors and wherein the recorded data collected during a flow filtration process is sufficiently comprehensive to allow control of the flow filtration process.

64. The system of claim 63, wherein the sensors are selected from at least one of flow rate sensors, pressure sensors, concentration sensors, pH sensors, conductivity sensors, temperature sensors, turbidity sensors, ultraviolet absorbance sensors, fluorescence sensors, refractive index sensors, osmolarity sensors, dried solids sensors, near infrared light sensors, or Fourier transform infrared light sensors.

65. The system of claim 55, wherein the first module includes a permeate recycling line for returning permeate to the inlet side of the first module, and wherein the modules subsequent to the first module each comprise a permeate recycling line for returning permeate to the inlet side of the same module and a permeate recirculation line for backfeeding permeate to a directly preceding module, and

wherein the system further comprises:

a first heat exchanger in thermal contact with the permeate withdrawal line of the first module,

a second heat exchanger in thermal contact with at least one permeate recirculation line of the subsequent modules,

a coolant supply line in fluid communication with at least one of the first and second heat exchangers.

66. The system of claim 55, wherein a permeate flow line of each of the subsequent modules after the first module comprises:

i) a respective recirculation line backfeeding the inlet side of a directly preceding module within the system, and ii) a respective tap line for diverting permeate flow from the recirculation line for withdrawal from the system.

67. The system of claim 56, further comprising blending control for withdrawn permeate flows of the first module and one or more of the subsequent modules effective to provide a product having a targeted overall purity.

68. The system of claim 56, wherein the retentate flow line from the first module and at least one of the subsequent modules is configured to backfeed retentate from the retentate exit of a module to the inlet side of an immediate subsequent module within the system.

69. The system of claim 56, wherein each filter comprises a microfiltration membrane.