초록 ▼

Continuous stream ratio blending of two or more liquids. Each stream flow is time synchronized to all others and turned on and off to dose precise ratios into a constant pressure streams combining chamber. Combined on-off flows constitute a net flow rate exceeding some maximum continuous flow dema

Continuous stream ratio blending of two or more liquids. Each stream flow is time synchronized to all others and turned on and off to dose precise ratios into a constant pressure streams combining chamber. Combined on-off flows constitute a net flow rate exceeding some maximum continuous flow demand for the blended liquids. Dosed streams are pumped from the streams combining chamber at a rate matching their inflow, then through a mixing element into a finished blend tank. Use of a constant pressure streams combining chamber feeding a mix pump allows decoupling of individual streams ratio dosing flows and pressures one from another and from the combined stream. Blended liquid is available on demand as a continuous stream from the level controlled finished blend tank. The level sensor automatically starts and stops blended flow into the tank. Streams flow can be stopped upon completion of any dose cycle.

대표청구항 ▼

What is claimed is: 1. A method for the combining together of two or more liquids to form a batch or blend of desired mixture ratio or proportions, the method comprising the following steps: providing a common constant pressure streams combining chamber, a mix pump and one or mixing elements, and a

What is claimed is: 1. A method for the combining together of two or more liquids to form a batch or blend of desired mixture ratio or proportions, the method comprising the following steps: providing a common constant pressure streams combining chamber, a mix pump and one or mixing elements, and a final blend tank; flowing two or more streams of liquids of time synchronized ratio defined intermittent doses into the common constant pressure streams combining chamber; synchronously removing liquid from the combining chamber at a flow rate matching the summed flow rate of the doses flowing into the chamber, the removed liquid then flowing through the mixing elements; and receiving the mixed liquid in a final blend tank of desired capacity where the blended liquids are available for use on a continuous stream or outflow basis, at a rate up to a defined maximum. 2. The method as set forth in claim 1 wherein the separation of ratio dosing streams flows apart from combining and mixing flow allows absolute separation of ratio dosing pressures from mixing pressures, such that one cannot act upon or alter the other. 3. The method as set forth in claim 1 wherein the flow from any one stream or any combination of streams into the streams combining chamber does not alter or influence the pressure in the combining chamber. 4. The method as set forth in claim 1 wherein the flow rate of any one stream into the combining chamber is essentially unaffected by the flow rates of any other stream or combination of streams flowing into the combining chamber. 5. The method as set forth in claim 1 wherein the size or amount of the ratio dose of any one stream flowing into the combining chamber is essentially unaffected by the size or amount of the ratio dose of any other stream or combination of streams flowing into the combining chamber. 6. The method as set forth in claim 1 wherein flow through the mixing elements is caused by and controlled by the mixing pump only and not by any streams ratio dose flows. 7. The method as set forth in claim 1 wherein the pressure acting on the dose streams combining chamber is atmospheric pressure. 8. The method as set forth in claim 1 wherein the pressure acting on the dose streams combining chamber can be at a specified and controlled and maintained pressure above atmospheric pressure. 9. The method as set forth in claim 1 wherein the nature and configuration of any mixing element has no effect upon the flow rate or size or amount of any ratio dose stream flowing into the combining chamber. 10. The method as set forth in claim 1 wherein the summed flow rate of the ratio dosing streams entering into the combining chamber is substantially equivalent to and synchronous with the flow rate of the combined streams exiting from the combining chamber. 11. The method as set forth in claim 1 wherein rate of flow of streams entering the streams combining chamber is matched to the rate of flow of the liquid leaving the streams combining chamber by maintaining the liquid in the streams combining chamber at relatively constant level. 12. The method as set forth in claim 1 wherein streams ratio dosing pumps are provided for flowing the two or more streams of liquids of time synchronized ratio defined intermittent doses, and wherein any non-synchronous ratio dose flow between streams upon the start of or the completion of a synchronous flow ratio dose flow event is minimized or eliminated by matching the acceleration rates and deceleration rates of the streams ratio dosing pumps. 13. The method as set forth in claim 12 wherein flow meters are provided downstream of the streams ratio dosing pumps, and wherein a mathematical technique termed herein as formula inflation can allow resizing of streams ratio dose flow rates, if necessary, to better fit within the available flow meter operating flow rate parameters. 14. The method as set forth in claim 1 wherein any non-synchronous ratio dose flow caused by one stream beginning actual dose flow earlier in the common fixed dose time than other streams is minimized or eliminated by delaying the start of flow of that stream and then delivering the requisite total ratio dose in the remaining available common dose time. 15. The method as set forth in claim 1 wherein the flow of the ratio defined and synchronized streams through the mixing pump contributes to the streams combining and mixing due to the mixing action of the pump. 16. The method as set forth in claim 1 wherein priming of the system fluid flow pathway with liquids is accomplished by monitoring the level of the streams combining chamber as each stream flow pathway is charged, beginning with the largest ratio fraction stream. 17. The method as set forth in claim 1 wherein the operation of the streams ratio dosing portion is functionally linked to the streams combining and mixing portion by only a single control signal, which serves to synchronize and match streams ratio dosing flow with streams combining and mixing flow. 18. The method as set forth in claim 1 wherein the streams combining chamber may be closed to atmosphere and wherein a pressure sensor is provided, and wherein level control can be implemented by first establishing a defined gas pressure in the chamber between flow cycles, then closing the chamber prior to a synchronous streams ratio dose flow cycle, then measuring the chamber pressure during streams flow using a pressure sensor and using the pressure sensor measurement to give feedback loop control of the mix stage pump in order to hold the chamber pressure and thus level nearly constant such that falling pressure increases mix pump flow and increasing pressure reduces mix pump flow.