Abstract: The present invention provides a process for the biodegradation of at least one xenobiotic. The process includes the steps of providing a bioreactor with an aqueous phase comprising water and at least one microorganism that is capable of metabolizing the xenobiotic and degradation products of the xenobiotic. The bioreactor is then provided with an organic phase comprising a solid or liquid polymer having an affinity for the xenobiotic and the xenobiotic is added to the bioreactor. The polymer is operable to absorb portions of the xenobiotic so that the aqueous concentration of the xenobiotic is substantially non-toxic to the microorganisms. The microorganisms degrade the xenobiotic in the aqueous phase causing the xenobiotic in the solid or liquid polymer to diffuse into the aqueous phase for degradation by the microorganisms.

Abstract: A process for biodegradation of a xenobiotic. A process for biodegradation of a xenobiotic comprising the steps of: contacting an organic phase comprising the xenobiotic and at least one substantially water-immiscible organic solvent with an aqueous phase comprising water and a microorganism capable of metabolizing the xenobiotic; partitioning a portion of the xenobiotic from the organic phase to the aqueous phase such that the concentration of the xenobiotic in the aqueous phase is substantially non-toxic to the microorganism; and causing the microorganism to metabolize the xenobiotic in the aqueous phase.

Abstract: Living tissues, such as hybridoma cells or insect cells suspended in a water soluble gelling agent, are microencapsulated in a double polymeric membrane microcapsule. The inner membrane is of a high molecular weight cut-off to permit outward diffusion of the gelling agent and also expansion of the microcapsule before formation of the outer membrane which is a relatively lower molecular weight cut-off. The living cells in the dual membrane microcapsule may be grown to an intracapsular density which is significantly higher than that which can be achieved by using single-membrane capsules. The recovery of intracapsular protein product (produced by the encapsulated cells) is also significantly higher and the loss of product through the membrane wall markedly lower for the dual membrane capsule than for the single membrane capsule.

Abstract: A process for producing a variety of chemical products, e.g., ethanol, by fermentation in which the product is removed from the fermentation medium as it is formed by liquid-liquid extraction using an extractant for the product which is immiscible with water. The extractant employed is chosen from the following groups: (A) double bond unsaturated aliphatic alcohols having 12 or more carbon atoms; (B) saturated branched chain aliphatic alcohols having 14 or more carbon atoms or mixtures thereof; (C) double bond unsaturated aliphatic acids having 12 or more carbon atoms; (D) aliphatic and aromatic mono-, di- or tri-esters having 12 or more carbon atoms, other than dibutyl phthalate; (E) aliphatic noncyclic ketones and aliphatic aldehydes having 12 or more carbon atoms; and (F) mixtures of extractants from groups (A) to (E) above or mixtures of at least one of the above extractants and at least one other extractant.