A support frame for dust collection system including a drum filter and a filter cleaning system is disclosed where the frame includes a plurality of octagonal supports spaced apart from each other in an axial direction defining an octagon-shaped peripheral profile. A plurality of axial members extend between adjacent octagonal supports, and end covers are secured to the frame members with each cover including a first inlet opening and a second inlet opening. The support frame may be used in a modular dust collection with a plurality of modular segments of filter media segments secured to the frame and a filter cleaner segments corresponding to the filter media segments.

A system for treatment of a polluted effluent, includes an outer chamber configured to treat the polluted effluent in mixture with a purification slurry including particles of one or more catalysts and/or organoclays, or a mixture thereof. The outer chamber includes (i) a stirring unit consisting of an engine and a stirrer, configured to mix the polluted effluent and the purification slurry to prevent the particles from sinking without causing a turbulence, (ii) a membrane located at the top of the outer chamber through which a treated effluent passes, while preventing the particles of one or more catalysts and/or organoclays from exiting the outer chamber together with the treated effluent, (iii) a membrane cleaning system configured to remove and collect the particles of one or more catalysts and/or organoclays accumulated on the membrane, and re-introducing the particles back to the bottom of the outer chamber.

A filter CF1 for filtering dialysis fluid comprises the following: a housing 52 inside of which a filter material 51 is accommodated and which is vertically long; an introduction port 53 that is disposed in the lower part of the housing and that introduces dialysis fluid from an upstream-side flow path 23a; a filtered fluid lead-out port 54 through which filtered dialysis fluid, which has passed through the filter material, is lead out from the upper part of the housing to a downstream-side flow path 23b; and an unfiltered fluid lead-out port 55 through which unfiltered fluid is lead out from the upper part of the housing to a waste fluid flow path 57. When removing the filter from a dialysis fluid circuit 4, fluid is suctioned from the inside of the housing via the upstream-side flow path by using fluid suction means 64A, and a gas is caused to flow into the housing from at least either one of the waste fluid flow path and the downstream-side flow path by using gas inflow means 65. The fluid may be suctioned from the downstream-side flow path and the gas may be caused to flow in from the upstream-side flow path, or the fluid may be suctioned from the waste fluid flow path and the gas may be caused to flow in from the downstream-side flow path. Residual fluid in the filter can be reduced.

A process for the regeneration of a membrane wall in a distillation apparatus, wherein a distillation apparatus having one or more evaporation and condensation stages is provided, each evaporation and condensation stage having at least one flow channel conducting a liquid, said flow channel being at least partially confined by a vapor-permeable and liquid-impermeable membrane wall, wherein vapor emerging from the liquid passes through the membrane wall. The liquid is removed from the at least one flow channel, wherein, after the removal of the liquid, the membrane wall is surrounded on both sides by a gas atmosphere, but is still wetted with liquid, and this liquid is removed by adjusting the gas atmosphere surrounding the membrane wall such that the partial pressure of the liquid in the gas atmosphere is lower than the vapor pressure of the liquid wetting the membrane wall.

A regenerable organic contaminant controller includes a carbon hollow fiber module that includes a passage between an inlet and an outlet, on an opposite end of the carbon hollow fiber module from the inlet, such that organic contaminants in contaminated air flowing through the passage are desorbed into pores of the carbon hollow fiber module. The regenerable organic contaminant controller also includes wires coupled to the inlet of the carbon hollow fiber module and to the outlet of the carbon hollow fiber module. The wires heat the carbon hollow fiber module based on a flow of electricity through the wires. The heat causes release of the organic contaminants from the pores of the carbon hollow fiber module.

An isolation device includes an isolation chip assembly, a vacuum system, a frequency converting module, and a controller. The isolation chip assembly includes an isolation chip having a first chamber and a second chamber, a first oscillator mounted on the first chamber, and a second oscillator mounted on the second chamber. The frequency converting module causes the vacuum system to generate negative pressure in the first and the second chambers alternately. The controller controls the first and the second oscillators to operate when the vacuum system stops generating the negative pressure in the first chamber and in the second chamber. The first and the second oscillators respectively generate a first and a second oscillation wave when operating, a frequency of the first oscillation wave is greater than a frequency of the oscillation wave, an amplitude of the first oscillation wave is less than an amplitude of the second oscillation wave.

A gas sparger produces an intermittent flow of bubbles even if provided with a continuous gas flow. The sparger has a housing to collect a pocket of gas and a conduit to release some of the gas from the pocket when the pocket reaches a sufficient size. Optionally, a cover over an outlet from the conduit may break up or distribute the released gas. A large sparger for use with a commercial membrane module can comprise a plurality of smaller units.

A regenerable organic contaminant controller includes a carbon hollow fiber module that includes a passage between an inlet and an outlet, on an opposite end of the carbon hollow fiber module from the inlet, such that organic contaminants in contaminated air flowing through the passage are desorbed into pores of the carbon hollow fiber module. The regenerable organic contaminant controller also includes wires coupled to the inlet of the carbon hollow fiber module and to the outlet of the carbon hollow fiber module. The wires heat the carbon hollow fiber module based on a flow of electricity through the wires. The heat causes release of the organic contaminants from the pores of the carbon hollow fiber module.

A tubular membrane is provided with a vortex generator at an upstream end of the tubular membrane. A spacer with multiple vortex generators may be added to module having a plurality of tubular membranes. A cap over the spacer may have separate inlets for a feed water and gas mixture and recirculating retentate. A system for membrane filtration includes a tubular membrane, a vortex generator, a liquid pump, a gas pump, and a retentate recirculation loop. In a filtration process, a gas is pumped into a flow of a feed liquid to produce a two-phase flow wherein the liquid is the continuous phase. The two-phase flow passes through the vortex generator and through a lumen of the tubular membrane. A continuous gas phase forms in part of the lumen of the tubular membrane. Contaminants in the liquid may be biased towards the continuous gas phase.

A system for treatment of a polluted effluent includes an outer chamber and a computerized control system. The system is configured to treat an effluent/catalyst mixture that includes the polluted effluent in admixture with a purification slurry. The slurry includes particles of one or more catalysts and/or organoclays. The treatment of the effluent/catalyst mixture is carried out by contact between the particles of the catalysts and/or organoclays and the polluted effluent to mineralize or degrade pollutants in the polluted effluent.