Abstract:
A biomass generator useful for continuously growing and withdrawing bacteria to be used in a desired beneficial application, the generator having a bacteria growth chamber; water and nutrient inlet ports; upper and lower outlet ports; a recirculating pump withdrawing and reintroducing fluid to establish a vortex in the growth chamber while controlling foaming and pump cavitation; a low pressure air inlet line discharging air inside the growth chamber above the vortex; a fluid discharge line receiving bacteria-containing fluid from the upper outlet port of the growth chamber; a flush line discharging wash water into the fluid discharge line; and an electrical controller cooperating with solenoid-operated valves and a feeder mechanism to periodically introduce water and nutrients into the chamber, thereby simultaneously causing bacteria-containing fluid to be discharged from the growth chamber through the upper outlet port. A method for growing bacteria using the subject apparatus is also disclosed.
Abstract:
The invention relates to a device for the cultivation of cells in liquid columns measured on a millimetre scale. Said device comprises a container for receiving a liquid culture suspension of the cells, a mixing element for mixing the culture suspension in the container around a mixing axis. The container and/or the mixing element are configured in such a manner that the speed of the flow is modified either locally and/or temporally along a streamline or flow line around the mixing axis.
Abstract:
A bioreactor (200) for cultivating living cells in a liquid medium. In one embodiment, the bioreactor (200) has a substrate (230) having a first surface and an opposite second surface, defining a channel (202) therein, and a plurality of chambers (204) formed in the substrate, wherein each of the plurality of chambers (204) is adapted for receiving cells in a liquid medium and formed with an open end (262), an opposite closed end (264) and side walls, the open end (262) and the closed end (264) defining a depth, d, therebetween for the corresponding chamber (206), the sidewalls defining a width, w, therebetween for the corresponding chamber (206). As such formed, each chamber (206) is in fluid communication with the channel (202) through the open end of the chamber (206), and at least two of the plurality of chambers (206) have depths or widths the same or different form each other.
Abstract:
A simple, reliable, inexpensive, and efficient anaerobic digester for treating organic wastes at a shortened residence time is described. The anaerobic digester is a multi-chambered digester that can handle wastewater and sludge in a large volume at a high flow rate. The digester also allows collection of methane gas for use as an energy source. The reactor is based on a sequential series of reaction chambers in a design that does not require internal moving parts. The volume of the chambers is adjusted to control the relative residence time of the waste to select an anaerobic microorganism group or groups that can efficiently digest the waste presented to that chamber. Under most conditions, no addition of bacteria is necessary. The digester works efficiently using microbes native to the waste material. After the reaction chambers and just prior to leaving as effluent, a settling chamber is located to reclaim the microbes and remove additional solids. In one embodiment, the reactor comprises four sequential chambers. However, other chamber numbers and geometries will achieve the same result if the residence time in each chamber is properly adjusted. Neither pH nor temperature needed to be controlled. However, for a higher yield of methane, pH may be controlled from about 6 to about 8.
Abstract:
Sealed Tight is an integrated anaerobic digester and aquaculture filtering system for agricultural waste treatment. This systems retrofits existing waste containment facilities, resulting in an economical system for complete waste treatment that, due to its sealed design, protects the environment from contamination, even during flood situations. Thoroughly digested manure as created in this system is a superior, low-odor fertilizer. Aquatic plants used to filter overflow are excellent livestock feed; and stored biogas provides farms with a high level of energetic self-sufficiency.
Abstract:
The present invention comprises a novel culture methods and devices in which living cells or subcellular biocatalysts are immobilized by the opposition of forces. The immobilized cells or biocatalysts may be attached to support complexes that add to the resultant vector forces.
Abstract:
A portable cassette is disclosed, for use in receiving, maintaining and growing biological cells ex vivo without exposing the cells to the external environment. The portable cassette is used in combination with a processor instrument that facilitates an initial inoculation of the cassette with cells of the kind to be grown and to distribute those cells in a predetermined pattern (e.g., uniformly) throughout a cell growth chamber. Thereafter, the portable cassette is used in combination with an incubator instrument that incubates the cell growth chamber so that the cells are optimally expanded. The same processor instrument then is used to harvest the expanded cells from the portable cassette. Both instruments are configured to condition the portable cassette during stages of the cell growth process, without disturbing the cassette's sterile system.
Abstract:
A control method for operating aqueous Haematococcus spp., such as H. pluvialis, microorganism growth processes is disclosed which can maintain viable growth conditions of this microorganism which have heretofore not been easily reproduced in commercially valuable quantities. The primary control parameters are the degree of turbulence in the aqueous growth medium and the scale of the apparatus relative to the scale of the turbulent eddies in vessels which are partially filled with the aqueous medium directly affect conditions which are required for optimum growth: light exposure, nutrient supply, sedimentation rate, bulk temperature, gas exchange rate and cell integrity. These control elements can be cast in terms of the Reynolds number (N.sub.re), pH, temperature, amount of impinging light, and NO.sub.2 concentration, depending upon the operative chlorophyll growth stages of Haematococcus spp. and its photoadaptive stages of producing astaxanthin.
Abstract:
A system for continuous perfusion culturing of anchorage-dependent and anchorage-independent mammalian cell lines, inter alia, wherein in vivo capillary bed conditions are simulated by providing a bioreactor having a growth chamber wherein the cells are grown between a multitubular array comprising at least three functionally separate, inert non-degradable and structurally strong tubes or sets of tubes. A constant nutrient gradient is maintained along the entire length of the tubes by perfusing medium through the tubes at a flow rate which is sufficient to expose all areas of the chamber to fresh medium by convective forces rather than diffusion. Oxygen transfer and removal of toxic wastes is improved by the invention herein. In a preferred embodiment, porous inert expanded Teflon tubes are employed having an inner diameter of approximately between 1 and 2 millimeters.
Abstract:
The invention aims at replacing animal experiments for determining acute toxicity (LD.sub.50 values) by utilizing stable perfusion-cultivated cell cultures and also at producing a cultivation chamber which is movable during operation, for determining various parameters.