Chloride measurement using non-harsh reagents
US-10670573-B2 · Jun 2, 2020 · US
US10648957B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10648957-B2 |
| Application number | US-201715851776-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 22, 2017 |
| Priority date | Dec 22, 2016 |
| Publication date | May 12, 2020 |
| Grant date | May 12, 2020 |
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A benchtop device flow setup for determining the effectiveness of magnetic treatment of feed water for reducing mineral scaling includes two similar branches, both equipped with a reverse osmosis membrane and a pump that operate in the transient regime at the same flow rate and transmembrane pressure. The flow setup is further fed with a solution at the same level of supersaturation measured in a stirred reactor, however, only one branch exposes the feed to a magnetic field.
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The invention claimed is: 1. A method for benchtop evaluation of effectiveness of a water treatment modality, comprising: a. providing a benchtop reverse osmosis (RO) system including RO membranes that operate in a transient regime of crossflow filtration for treated and untreated feed water, b. measuring kinetics of precipitation of a supersaturated solution in a stirred reactor based on at least one feed characteristic; and c. characterizing the solution supersaturation based on the at least one solution characteristic during a certain period of time and a total relative change of the characteristic at a beginning and an end of the precipitation process; wherein flow through the RO system is a single-pass flow, and wherein the testing is performed using a flow setup that includes two similar branches, both equipped with an RO membrane and a pump that are operating in the transient regime at the same flow rate and transmembrane pressure and fed with a solution at the same level of supersaturation measured in the stirred reactor, wherein only one branch exposes the feed to a magnetic field. 2. The method of claim 1 , wherein the feed characteristic is selected from a group consisting of electrical conductivity, turbidity, and concentrations of ions of sparingly soluble salts. 3. The method of claim 1 , wherein at least one of polarized microscopy with image processing software, scanning electron microscopy (SEM), X-ray diffractometry (XRD), and differential scanning calorimetry (DSC) is used to characterize the scale formed on the RO membrane. 4. The method of claim 1 , wherein the evaluation is completed within a period of between about 10 minutes and 30 minutes. 5. A method for benchtop evaluation of effectiveness of a water treatment modality, comprising: a. providing a benchtop reverse osmosis (RO) system including RO membranes that operate in a transient regime of crossflow filtration for treated and untreated feed water, b. measuring kinetics of precipitation of a supersaturated solution in a stirred reactor based on at least one feed characteristic; and c. characterizing the solution supersaturation in the benchtop reverse osmosis (RO) system based on the at least one solution characteristic during a certain period of time and a total relative change of the characteristic at a beginning and an end of the precipitation process; wherein flow through the RO system is a single-pass flow, and wherein the characterizing step includes characterization of solution supersaturation based at least in part on a parameter ξ(t) that is calculated as the ratio between a change in one of said feed characteristics during a period of time t and the total change so that ξ=0 and ξ=1 are at the beginning and the end of the precipitation process, respectively. 6. An apparatus for evaluating effectiveness of a water treatment modality, comprising: a. a benchtop reverse osmosis (RO) system that includes RO membranes that operate in a transient regime of crossflow filtration for treated and untreated feed water, wherein flow through the RO system is a single-pass flow; b. means associated with the benchtop RO system for measuring kinetics of precipitation of a supersaturated solution in a stirred reactor based on at least one feed characteristic; and c. means associated with the benchtop RO system for characterizing the solution supersaturation based on the at least one solution characteristic during a certain period of time and a total relative change of the characteristic at a beginning and an end of the precipitation process; wherein the testing is performed using a flow setup that includes two similar branches, both equipped with an RO membrane and a pump that are operating in the transient regime at the same flow rate and transmembrane pressure and fed with a solution at the same level of supersaturation measured in the stirred reactor, wherein only one branch exposes the feed to a magnetic field. 7. The apparatus of claim 6 , wherein the feed characteristic is selected from a group consisting of electrical conductivity, turbidity, and concentrations of ions of sparingly soluble salts. 8. The apparatus of claim 6 , wherein at least one of polarized microscopy with image processing software, scanning electron microscopy (SEM), X-ray diffractometry (XRD), and differential scanning calorimetry (DSC) is used to characterize the scale formed on the RO membrane. 9. The apparatus of claim 6 , wherein the evaluation is completed within a period of between about 10 minutes and 30 minutes. 10. An apparatus for evaluating effectiveness of a water treatment modality, comprising: a. a benchtop reverse osmosis (RO) system that includes RO membranes that operate in a transient regime of crossflow filtration for treated and untreated feed water, wherein flow through the RO system is a single-pass flow; b. means associated with the benchtop RO system for measuring kinetics of precipitation of a supersaturated solution in a stirred reactor based on at least one feed characteristic; and c. means associated with the benchtop RO system for characterizing the solution supersaturation based on the at least one solution characteristic during a certain period of time and a total relative change of the characteristic at a beginning and an end of the precipitation process; wherein the characterizing step includes characterization of solution supersaturation based at least in part on a parameter ξ(t) that is calculated as the ratio between a change in one of said feed characteristics during a period of time t and the total change so that ξ=0 and ξ=1 are at the beginning and the end of the precipitation process, respectively.
Turbidity · CPC title
Water · CPC title
Control or steering systems not provided for elsewhere in subclass C02F · CPC title
Aggregation, sedimentation, flocculation, precipitation or coagulation · CPC title
Specific process operations in the feed stream; Feed pretreatment · CPC title
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