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A process for the continuous production of a mixture of substances or of a reaction mixture that has been formed by reaction of components contained therein. The component streams withdrawn from a storage container (1, 2 or 3) or a distribution network (12) are each conveyed via a controlled system

A process for the continuous production of a mixture of substances or of a reaction mixture that has been formed by reaction of components contained therein. The component streams withdrawn from a storage container (1, 2 or 3) or a distribution network (12) are each conveyed via a controlled system (22, 23, 24, 25) which in each instance comprises a flow-measuring device (8, 9, 10, 11) and a regulating element (34, 35, 36, 37). The flow-rates of the individual components are regulated in quantitatively proportional manner with reference to the flow-rate of a first component. The resulting regulated flow-rates are introduced into a receiving container, either directly or after individual flow-rates have been completely or partially conducted together. The process and the device are especially suitable for the on-site production of mixtures of substances that cannot be transported or that can only be transported in elaborate manner, such as relatively highly concentrated solutions of peroxycarboxylic acid.

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A process for the continuous production of a mixture of substances or of a reaction mixture that has been formed by reaction of components contained therein. The component streams withdrawn from a storage container (1, 2 or 3) or a distribution network (12) are each conveyed via a controlled system

A process for the continuous production of a mixture of substances or of a reaction mixture that has been formed by reaction of components contained therein. The component streams withdrawn from a storage container (1, 2 or 3) or a distribution network (12) are each conveyed via a controlled system (22, 23, 24, 25) which in each instance comprises a flow-measuring device (8, 9, 10, 11) and a regulating element (34, 35, 36, 37). The flow-rates of the individual components are regulated in quantitatively proportional manner with reference to the flow-rate of a first component. The resulting regulated flow-rates are introduced into a receiving container, either directly or after individual flow-rates have been completely or partially conducted together. The process and the device are especially suitable for the on-site production of mixtures of substances that cannot be transported or that can only be transported in elaborate manner, such as relatively highly concentrated solutions of peroxycarboxylic acid. layer positioned within the housing. The first filter layer absorbs contaminants from stormwater to produce a first treated stormwater having an effluent concentration that meets the USEPA Water Quality Criteria when stormwater permeates the first layer. The second filter layer precipitates substantially all of the dissolved contaminants remaining in the first treated stormwater when the first treated storm water permeates through the second filter layer. he wall to counteract lower flow resistance in proximity to the outlet of the water filter to result in a more uniform flow of water through the filter screen exiting through the outlet of the water filter. 7. The improvement of claim 1 where the filter screen and filter chamber each have a bottom as defined by the direction of gravity and the cone basin is coupled to the bottom of the filter chamber and is disposed adjacent to a bottom of the filter screen, where the cone basin comprises a cone and a basin each with a top and a bottom, which cone is coupled to the top of the basin, the cone extends upwardly into the filter screen, so that rotating water is forced toward a larger radius of movement by the cone, thereby serving to impart a higher centrifugal force to particles entrained in the water to separate out and trap the particles into the basin. 8. The improvement of claim 7 further comprising a narrow annulus with a small cross-sectional area formed between the bottom of the cone and the top of the basin, wherein the basin comprises a flush tube to flush out particles collected in the basin and to induce a high velocity flow through the narrow annulus. 9. A fluid filter comprising: a y-branched filter chamber having an inlet and an outlet, and a top and a bottom defined by gravitational orientation; a spin plate disposed in the filter chamber and having a first longitudinal axis; a filter screen having a second longitudinal axis, a top and a bottom as defined by gravitational orientation and an interior supplied with fluid from the spin plate and disposed in the filter chamber, the first and second longitudinal axes being collinear; a flow distributing sleeve disposed in the filter chamber outside of the filter screen and having an inlet and proximal side; and an end cap having a top extending into the bottom of the interior of the filter screen; wherein the spin plate comprises fluid passageways disposed therethrough at an approximal 20 degree angle azimuthally inclined relative to the second longitudinal axis of the filter screen; wherein the flow distribution sleeve comprises a plurality of axial slots which are narrower at the proximal side and wider at the distal side; wherein the end cap is coupled to the bottom of the filter chamber and disposed adjacent to a bottom of the filter screen, and wherein the end cap is comprised of a cone with a top and a bottom as defined by gravitational orientation and a basin with a top and a bottom as defined by gravitational orientation in which the cone is coupled to the top of a basin, where the top of the cone forms the top of the end cap which extends upwardly into the interior of the filter screen, where a narrow annulus with a small cross-sectional area is defined between the bottom of the cone and the top of the basin, where the basin comprises an openable flush tube to flush out particles collected in the basin and to induce a high velocity flow through the annulus when the flush tube is opened. 10. A high volume fluid filter comprising: a filter chamber means for providing a gravitationally oriented filtration space having an inlet and an outlet; a cylindrical filter screen means for filtering out particles, the filter screen means being disposed within the filter chamber means; a spin plate means disposed in fluidic communication to the inlet for defining fluid jets at an oblique angle relative to the filter screen so that particles entrained in the flow obliquely flow against the filter screen means; a flow distributing sleeve means for distributing flow across the filter screen means according to a predetermined pattern; and a cone basin means for collecting the particles. 11. The fluid filter of claim 10 where the filter screen means has a longitudinal axis and where said fluid jets are azimuthally directed at approximately a 20 degree angle relative to the longitudinal axis of the filter screen means. 12. The fluid filter of claim 1 where the