A gas solution manufacturing device 1 includes a gas supply line 2 configured to supply a gas as a raw material of a gas solution, a liquid supply line 3 configured to supply a liquid as a raw material of the gas solution, a gas solution production unit 4 configured to mix the gas and the liquid together to produce the gas solution, a gas-liquid separation unit 5 configured to perform gas-liquid separation of the produced gas solution into a supplied liquid to be supplied to a use point and a discharged gas to be discharged through an exhaust port, and a gas dissolving unit 6 provided in the liquid supply line 4 and configured to dissolve the discharged gas resulting from the gas-liquid separation in the liquid. The gas dissolving unit 6 is configured with a hollow fiber membrane configured with a gas permeable membrane.

To provide biotechnological filtration possibilities with which the danger of contamination is low and at the same time an optimum flow profile can be achieved, the use of a filter module 100 is proposed, the latter having, in a filter housing 110, a filter, with a bundle of hollow fibres 114, and a centrifugal pump rotor 132, for a biotechnological production method, and a filter module 100 for the filtration of a biotechnological liquid L, having a filter housing 110, a filter arranged in the filter housing 110 with a bundle of hollow fibres 114, a centrifugal pump rotor 132 arranged in the filter housing 110 such that it is fluidically connected to the interior of the hollow fibres 114, wherein the centrifugal pump rotor 132 is able to be magnetically driven such that it can force a liquid L through the hollow fibres 114, a first port 102 for the supply of a biotechnological liquid L to be filtered, which first port 102 is fluidically connected to the interior of the hollow fibres 114 of the filter, a second port 104 for the removal of a biotechnological liquid L to be filtered, which second port 104 is fluidically connected to the interior of the hollow fibres 114 of the filter, and a third port 107 for the removal of precipitated waste liquid, which third port 107 is fluidically connected to the exterior of the hollow fibres 114, and a filtration device 1100, 1200, 1300 having a filter module 100, which is able to be coupled to a drive unit, and a drive unit for magnetically driving the centrifugal pump rotor 132 of the filter module 100, which drive unit can generate dynamic magnetic fields for magnetically driving and magnetically supporting the centrifugal pump rotor 132 when the filter module 100 is coupled to the drive module.

Provided herein are, inter alia, biological manufacturing and downstream purification processes.

A detonator positioning device for use with a detonator in a perforating gun assembly is described. The detonator positioning device is configured for electrically contactably forming an electrical connection within the perforating gun housing by contact. The detonator positioning device includes a body having a first end, a second end, and a central bore extending between the first and second ends. The central bore is adapted for receiving one or more electrically contactable components of a detonator. The detonator positioning device aligns at least one of the one or more electrically contactable components to form an electrical connection with a bulkhead assembly.

This application relates to a method of treating wastewater wherein an oxygen infusion system is used to supersaturate wastewater before aerobic biological processes, wherein oxygen is transferred to the wastewater free of oxygen bubbles and achieves a reduction in power demand for the aeration process of wastewater.

The present invention provides a method for producing lipid particles that have a desired particle diameter, the method comprising: (A) a step for preparing, in a first mixing region, a primary dilution by mixing a first solution containing a lipid and an alcohol with a second solution containing water; (B) a step for feeding the primary dilution from the first mixing region to a second mixing region through a liquid feed pipe within a prescribed time; and (C) a step for preparing a secondary dilution by mixing the primary dilution with a third solution containing water in the second mixing region, wherein the steps (A)-(C) are continuously carried out, and the particle diameter of the lipid particles is controlled by adjusting at least one condition selected from the group consisting of the concentration of the alcohol and the concentration of the lipid in the primary dilution, the prescribed time, and the temperature during mixing.

The present invention provides a method for producing lipid particles that have a desired particle diameter, the method comprising: (A) a step for preparing, in a first mixing region, a primary dilution by mixing a first solution containing a lipid and an alcohol with a second solution containing water; (B) a step for feeding the primary dilution from the first mixing region to a second mixing region through a liquid feed pipe within a prescribed time; and (C) a step for preparing a secondary dilution by mixing the primary dilution with a third solution containing water in the second mixing region, wherein the steps (A)-(C) are continuously carried out, and the particle diameter of the lipid particles is controlled by adjusting at least one condition selected from the group consisting of the concentration of the alcohol and the concentration of the lipid in the primary dilution, the prescribed time, and the temperature during mixing.

A dialyzer, a dialysis machine, a kit and a process for producing the dialyzer. The dialyzer includes a plurality of hollow fibers disposed in a housing of the dialyzer. The hollow fibers are wrapped with a textile fabric that is fluid-permeable and/or at least partly water-soluble.

A computer-implemented method for designing and assessing the performance of a hollow fibre membrane contactor (MBC) in a natural gas sweetening process using a MBC model is described in an embodiment. The MBC model comprises model parameters, model equations and boundary conditions for calculating data associated with the natural gas sweetening process. The natural gas sweetening process comprises removal of acid gas from natural gas using a solvent comprising at least one component. The method comprises: (i) forming a regression model using empirical data; (ii) determining a Henry's constant of CO.sub.2 in the solvent using the regression model; (iii) inputting the determined Henry's constant of CO.sub.2 in the MBC model as one of the model parameters; and (iv) determining CO.sub.2 absorption in the solvent using the MBC model for designing and assessing the performance of the MBC.

The invention relates to a method and apparatus for treatment of produced or process water from hydrocarbon production to reduce the volume of the produced or process water while simultaneously reducing the salinity of a highly saline stream, for example, the brine from a seawater desalination plant. The method includes causing a feed stream comprising produced or process water to flow through the lumen of a hollow fiber osmotic membrane 4 which is immersed in an open channel 2 or tank of flowing draw solution 6 which has high salinity. In this way, water from the feed stream is drawn through the osmotic membrane 4 by an osmotic pressure differential caused by the difference in salinity between the feed stream and the draw solution 6.