A feasibility study of a filtration type autotransfusion device

Bioengineering the liver: scale-up and cool chain delivery of the liver cell biomass for clinical targeting in a bioartificial liver support system

Acute liver failure has a high mortality unless patients receive a liver transplant; however, there are insufficient donor organs to meet the clinical need. The liver may rapidly recover from acute injury by hepatic cell regeneration given time. A bioartificial liver machine can provide temporary liver support to enable such regeneration to occur. We developed a bioartificial liver machine using human-derived liver cells encapsulated in alginate, cultured in a fluidized bed bioreactor to a level of function suitable for clinical use (performance competence). HepG2 cells were encapsulated in alginate using a JetCutter to produce ∼500 μm spherical beads containing cells at ∼1.75 million cells/mL beads. Within the beads, encapsulated cells proliferated to form compact cell spheroids (AELS) with good cell-to-cell contact and cell function, that were analyzed functionally and by gene expression at mRNA and protein levels. We established a methodology to enable a ∼34-fold increase in cell density within the AELS over 11-13 days, maintaining cell viability. Optimized nutrient and oxygen provision were numerically modeled and tested experimentally, achieving a cell density at harvest of >45 million cells/mL beads; >5×10(10) cells were produced in 1100 mL of beads. This process is scalable to human size ([0.7-1]×10(11)). A short-term storage protocol at ambient temperature was established, enabling transport from laboratory to bedside over 48 h, appropriate for clinical translation of a manufactured bioartificial liver machine.

Activation of the complement system by different autologous transfusion devices: an in vitro study

BACKGROUND

The aim of the present investigation was to study whether autologous transfusion devices activate the complement system and whether complement-activated blood is more vulnerable to further activation during processing.

STUDY DESIGN AND METHODS

Forty-eight blood units were randomized to be processed by one of three different salvage systems: Group 1 underwent whole blood filtration (hemofiltration) (n=16); Group 2 underwent continuous processing, saline washing, and centrifugation (CATS, Fresenius AG ) (n=16); and Group 3 underwent saline washing and centrifugation (Cell-Saver, Haemonetics Corp.) (n=16). Eight blood units for each system were activated with cobra venom factor (CVF) at a concentration of 0.2 U per mL whole blood before processing. C activation was studied by determinations of C4d, Bb, C3a, and SC5b-9. Samples were drawn from whole blood, processed blood, and the waste bags.

RESULTS

The concentrations of Bb, C3a, and SC5b-9 in whole blood after activation with CVF were significantly elevated compared to blood that was not activated (p < 0.01). Processed blood from hemofiltration contained significantly higher levels of complement-split products than techniques that use washing and centrifugation. The concentrations of SC5b-9 in blood processed by hemofiltration were higher in the experiments with CVF activation (p < 0.05).

CONCLUSION

The tested autologous transfusion systems did not themselves activate the complement system, and complement-activated blood was not more vulnerable to further activation during processing. A blood-salvaging technique that used washing and centrifugation reduced elevated concentrations of complement-split products, whereas hemofiltration did not.

In vitro evaluation study of the membrane autotransfusion system experimental prototype: MATS-I

Membrane Autotransfusion System (MATS) utilizing plasmapheresis technology has been developed in our laboratory. A specially designed polyethylene hollow fiber membrane was utilized. This study was conducted to evaluate performance of the first experimental prototype, MATS-I. The results of this study showed that the MATS-I could concentrate diluted blood at 10% of the initial hematocrit concentration (HCTi) into over 40% after passing through the system at a transmembrane pressure of 70 mm Hg. Moreover, the MATS-I can continuously treat 10,000 ml of diluted blood at various HCTi levels without deteriorating its performances. Even though the MATS-I met all required performances as an autotransfusion system, several areas of improvement of the system were necessary to meet various clinical needs. The next prototype, MATS-II, can be designed based on experiences obtained from the MATS-I. The MATS is smaller, more atraumatic and continuous, and is a faster system when compared to the currently available centrifugal autotransfusion devices.