Example 2
548.7 g Keystone™ liquid pyranine solution and 100.1 g of 1-propanol were charged to a 1 L multi-neck round bottom flask equipped with mechanical agitator, thermocouple, methallyl chloride dosing line, NaOH, 50% dosing line, and condenser. The mixture was heated to 70° C. and upon reaching the reaction temperature slow additions of methallyl chloride and NaOH, 50% were begun. The reaction mixture was refluxed at 70-72° C. during the addition. The methallyl chloride was added over 4 hours while the 50% NaOH was added over 6 hr period. After completion of the NaOH, 50% addition, the reaction mixture was held at 70° C. for 2 more hours. No distillation or other isolation steps were performed on the reaction product.
Table 3 summarizes the material balance of the initial reaction mixture.
TABLE 3
Material balance
EW
MaterialWt (g)Wt %(g/eq)moles
Pyranine solution548.778.012280.000.241
(calculated as 23%)*
NaOH, 50%25.63.64800.320
Methallyl chloride29.04.1290.550.320
1-propanol100.114.23——
Total703.4100.0
*Pyranine solution as supplied is 19-23% pyranine
Table 4 sets forth the composition of the reaction product as determined by NMR.
TABLE 4
Composition of Example 2 Reaction product
Reaction Product
ComponentMole %Weight %
methallyloxy pyranine52.281.5
methallyl pyranine6.19.5
Methallyl Alcohol34.86.8
Dimethallyl Ether2.80.9
2-methyl-3-propoxyprop-1-ene4.21.3
No unfunctionalized pyranine was detected by NMR. The unfunctionalized pyranine content was 0.11 wt % of the final solution as determined by LC. The unfunctionalized pyranine content was 0.55 wt % (0.61 mol %) of the total of pyranine, methallyl oxy pyranine and methallyl pyranine.
Example 3
Example 2 was repeated, but 2-propanol was used instead of 1-propanol. The unfunctionalized pyranine content was 0.50 wt % (0.55 mol %) of the total of unfunctionalized pyranine, methallyl oxy pyranine and methallyl pyranine, as determined by NMR.
Example 5
247 g of water was added to a round bottom flask. Next, 66.1 g of maleic anhydride was added with stirring. 27 g of 50% sodium hydroxide was then added along with 0.0616 g of ferrous ammonium sulfate hexahydrate. The initial charge was heated to 85° C. A monomer mixture containing 125.3 g of acrylic acid, 11.9 g of methyl methacrylate, 74 g of AMPS 2403 from Lubrizol (50% AMPS) and 22.5 g of the liquid reaction product from Example 2, (which contains 1.88 g of methallyl oxy pyranine, 0.1 mole percent of the monomer mixture) was added over 4 hours. Simultaneously, an initiator solution containing 15.3 g of sodium persulfate, 50.9 g of 35% hydrogen peroxide dissolved in 25 g of water was added over the same period of 4 hours. The reaction mixture was held for one hour at 85° C. The reaction mixture was then cooled down to room temperature and 50.4 g of 50% sodium hydroxide was added. The polymer solution contained approximately 40% polymer solids and a pH of 4.5.
Example 6
Pyranine solution, 19-23% in water (553.9 g, Milikin), 1-propanol (100.0 g) and sodium hydroxide, 50% (25.88 g) were charged to a 1-L multi-neck round bottom flask equipped with mechanical agitator, thermocouple, methallyl chloride dosing line, and condenser. The mixture was heated to 70° C. and upon reaching the reaction temperature a flow of methallyl chloride begun (0.13 mL/min, 247 minutes, 34.71 g) and the reaction mixture refluxed at 70-72° C. during the addition. After completion of the methallyl chloride addition, the mixture was digested for a 4 hr period at 70° C. The reaction mixture was cooled and discharged (700 g). Table 6 summarizes the material balance and Table 7 the analysis of the sample compared to the sample made by co-dosing the sodium hydroxide and methallyl chloride to the pyranine solution.
TABLE 6
Material balance of Example 6
EW
MaterialWt(g)Wt %(g/eq)moles
Pyranine solution, 19-23%553.978.072280.000.243
NaOH, 50%25.93.65800.324
Methallyl chloride29.74.1890.550.328
1-propanol100.014.09——
TABLE 7
NMR analysis of co-dosing process
Ex. 6Ex. 6
(NaOH(NaOH
addedaddedEx. 2Ex. 2
upfront)upfront)(co-dosing)(co-dosing)
ComponentWeight %Mole %Weight %Mole %
methallyl oxy79.148.481.552.2
Pyranine
Unreacted1.61.1NDND
Pyranine
Methallyl8.039.06.834.8
Alcohol
Dimethallyl0.72.10.92.8
Ether
methallyl9.55.89.55.8
Pyranine
2-methyl-3-1.23.61.34.2
propoxyprop-1-ene
As seen in Table 7, the co-dosing method gives higher amounts of pyranine reaction product along with reducing the amount of unreacted pyranine to below the detection limit of NMR of ˜1 mol %. A higher rate of methallyl alcohol formation is likely the cause of the lower conversion for the process in which the NaOH is added upfront. This hypothesis is supported by the higher amount of methallyl alcohol seen in the NMR analysis. The method of Example 2 achieved higher conversion of pyranine to polymerizable monomers than the method of Example 6.
Example 7
An initial charge of 248 g deionized water and 66 g of maleic anhydride was added to a 1-liter glass reactor with inlet ports for an agitator, water cooled condenser, thermocouple, and adapters for the addition of monomer and initiator solutions. The reactor contents were heated 85° C. 27 g of 50% sodium hydroxide and 0.0616 g of ferrous ammonium sulfate hexahydrate was added. A mixed monomer solution which consisted of 125.5 g of acrylic acid, 11.9 g of methyl methacrylate, 74.3 g of AMPS 2403 (50% solution of sodium AMPS from Lubrizol) 8.13 g of the monomer solution from Example 2 was fed to the reactor via measured slow-addition with stirring over a period of 4 hours. An initiator solution of 50.9 g of 35% hydrogen peroxide, 15.2 grams sodium persulfate dissolved in 25 grams water was concurrently added, starting at the same time as the monomer solution, for a period of 4 hours. The reaction product was then held at 85° C. for 30 minutes. Next, 0.36 g of erythorbic acid dissolved in 3 g of water was added. Immediately after that, 0.36 g of tertiary butyl hydroperoxide, 70% solution dissolved in 3 g of water was added. The reaction mixture was then heated at 85° C. for 1 hour. The polymers partially neutralized with 50.4 g of 50% sodium hydroxide. The final reaction mixture was an amber colored solution with a solids of about 40%, and a pH of 4.4.
Example 8
An initial charge of 248 g deionized water and 66 g of maleic anhydride was added to a 1-liter glass reactor with inlet ports for an agitator, water cooled condenser, thermocouple, and adapters for the addition of monomer and initiator solutions. The reactor contents were heated 85° C. 27 g of 50% sodium hydroxide and 0.0616 g of ferrous ammonium sulfate hexahydrate was added. A mixed monomer solution which consisted of 125.5 g of acrylic acid, 11.9 g of methyl methacrylate, 74.3 g of AMPS 2403 (50% solution of sodium AMPS from Lubrizol) 22.35 g of the monomer solution from Example 2 was fed to the reactor via measured slow-addition with stirring over a period of 4 hours. An initiator solution of 50.9 g of 35% hydrogen peroxide, 15.2 grams sodium persulfate dissolved in 25 grams water was concurrently added, starting at the same time as the monomer solution, for a period of 4 hours. The reaction product was then held at 85° C. for 30 minutes. Next, 0.36 g of erythorbic acid dissolved in 3 g of water was added. Immediately after that, 0.36 g of tertiary butyl hydroperoxide, 70% solution dissolved in 3 g of water was added. The reaction mixture was then heated at 85° C. for 1 hour. The polymers partially neutralized with 50.4 g of 50% sodium hydroxide. The final reaction mixture was an amber colored solution with a solids of about 40%, and a pH of 4.4.
Example 9
Various water treatment polymers were evaluated for their ability to prevent the precipitation of calcium carbonate in typical cooling water conditions, a property commonly referred to as the threshold inhibition. Solutions were prepared in which the ratio of calcium concentration to alkalinity was 1.000:1.448 to simulate typical conditions in industrial water systems used for cooling. Generally, water wherein the alkalinity is proportionately less will be able to reach higher levels of calcium, and water containing a proportionally greater amount of alkalinity will reach lower levels of calcium. Since cycle of concentration is a general term, one cycle was chosen, in this case, to be that level at which calcium concentrations equaled 100.0 mg/L Ca as CaCO3 (40.0 mg/L as Ca). The complete water conditions at one cycle of concentration (i.e., make-up water conditions) were as follows:
Simulated Make-Up Water Conditions:
-
- 100.00 mg/L Ca as CaCO3 (40.0 mg/L as Ca) (one cycle of concentration)
- 49.20 mg/L Mg as CaCO3 (12.0 mg/L as Mg)
- 2.88 mg/L Li as CaCO3 (0.4 mg/L Li as Li)
- 144.80 M Alkalinity (144.0 mg/L as HCO3)
- 13.40 P Alkalinity (16.0 mg/L as CO3)
In dynamic testing, where the pH is about 8.80, bulk water temperature is around 104° F., flow is approximately 3.0 m/s, and heat transfer is approximately 17,000 BTU/hr/ft2, above average threshold inhibitors can reach anywhere from four to five cycles of concentration with this water before significant calcium carbonate precipitation begins. Average threshold inhibitors may only be able to reach three to four cycles of concentration before precipitating, while below average inhibitors may only reach two to three cycles of concentration before precipitation occurs.
Polymer performance is generally expressed as percent calcium inhibition. This number is calculated by taking the actual soluble calcium concentration at any given cycle, dividing it by the intended soluble calcium concentration for that same given cycle, and then multiplying the result by 100. Resulting percentage amounts that are below 90% calcium inhibition are considered to be indicators of a significant precipitation of calcium carbonate. However, there are two ways in which an inhibitor can react once the threshold limit is reached. Some lose practically all of their calcium carbonate threshold inhibition properties, falling from 90-100% to below 25% threshold inhibition. Others are able to “hold on” better to their inhibition properties, maintaining anywhere from 50% to 80% threshold inhibition.
Testing beyond the threshold limit in order to determine each inhibitor's ability to “hold on” has been found to be a better method of predicting an inhibitor's ability to prevent the formation of calcium carbonate in the dynamic testing units. It also allows for greater differentiation in test results. Therefore, a higher cycle (4.0 cycles) was chosen for this test. At this concentration, above average inhibitors should be expected to give better than 60% threshold inhibition. Poor inhibitors should be expected to give less than 20% threshold inhibition, while average inhibitors should fall somewhere in between.
Materials:
-
- One incubator/shaker, containing a 125 mL flask platform, with 34 flask capacity
- 34 Screw-cap Erlenmeyer Flasks (125 mL)
- 1 Brinkmann Dispensette (100 mL)
- Deionized Water
- Electronic pipette(s) capable of dispensing between 0.0 mL and 2.5 mL
- 250 Cycle Hardness Solution*
- 10,000 mg/L treatment solutions, prepared using known active solids of the desired treatment*
- 10% and 50% solutions of NaOH
- 250 Cycle Alkalinity Solution*
- 0.2 μm syringe filters or 0.2 μm filter membranes
- 34 Volumetric Flasks (100 mL)
- Concentrated Nitric Acid * See solution preparations in next section.
Solution Preparations:
All chemicals used were reagent grade and weighed on an analytical balance to ±0.0005 g of the indicated value. All solutions were made within thirty days of testing. The hardness, alkalinity, and 12% KCl solutions were prepared in a one liter volumetric flask using DI water. The following amounts of chemical were used to prepare these solutions—
250 Cycle Hardness Solution:
-
- 10,000 mg/L Ca⇒36.6838 g CaCl2·2H2O
- 3,000 mg/L Mg⇒25.0836 g MgCl2·6H2O
- 100 mg/L⇒Li 0.6127 g LiCl
250 Cycle Alkalinity Solution:
-
- 36,000 mg/L HCO3⇒48.9863 g NaHCO3
- 4,000 mg/L CO3⇒7.0659 g Na2CO3
10,000 mg/L Treatment Solutions:
Using percentage of active product in the supplied treatment, 250 mL of a 10,000 mg/L active treatment solution was made up for every treatment tested. The pH of the solutions was adjusted to between 8.70 and 8.90 using 50% and 10% NaOH solutions by adding the weighed polymer into a specimen cup or beaker and filling with DI water to approximately 90 mL. The pH of this solution was then adjusted to approximately 8.70 by first adding the 50% NaOH solution until the pH reached 8.00, and then by using the 10% NaOH until the pH equaled 8.70. The solution was then poured into a 250 mL volumetric flask. The specimen cup or beaker was rinsed with DI water and this water was added to the flask until the final 250 mL was reached. The amount of treatment product to be weighed was calculated as follows:
Test Setup Procedure:
The incubator shaker was turned on and set for a temperature of 50° C. to preheat. 34 screw cap flasks were set out in groups of three to allow for triplicate testing of each treatment, allowing for testing of eleven different treatments. The one remaining flask was used as an untreated blank.
The Brinkmann dispensette was calibrated to deliver 96.6 mL, using DI water, by placing a specimen cup or beaker on an electronic balance and dispensing the water into the container for weighing. The dispensette was adjusted accordingly, until a weight of 96.5-96.7 g DI water was delivered. This weight was recorded, the procedure was repeated for a total of three measurements, and the average determined. Once calibrated, 96.6 mL DI water was dispensed into each flask.
Using a 2.5 mL electric pipette, 1.60 mL of hardness solution was added to each flask to simulate four cycles of make-up water.
Using a 250 μL electronic pipette, 200 μL of desired treatment solution were added to each flask to achieve a 20 mg/L active treatment dosage. A new tip on the electric pipette was used for each treatment solution so cross contamination did not occur.
Using a 2.5 mL electric pipette, 1.60 mL of alkalinity solution was added to each flask to simulate four cycles of make-up water. The addition of alkalinity was done while swirling the flask, so as not to generate premature scale formation from high alkalinity concentration pooling at the addition site.
One “blank” solution was prepared in the exact same manner as the above treated solutions, except DI water was added in place of the treatment solution.
All 34 flasks uncapped were placed onto the shaker platform and the door closed. The shaker was run at 250 rpm and 50° C. for 17 hours.
A “total” solution was prepared in the exact same manner as the above treated solutions were prepared, except that DI water was used in place of both the treatment solution and alkalinity solution. This solution was capped and left overnight outside the shaker.
Test Analysis Procedure:
Once 17 hours had passed, the 34 flasks were removed from the shaker and allowed to cool for one hour. Each flask solution was filtered through a 0.2 μm filter membrane. The filtrate was analyzed directly for lithium, calcium, and magnesium concentrations by either an Inductively Couple Plasma (ICP) Optical Emission System or Flame Atomic Absorption (AA) system. The “total” solution was analyzed in the same manner.
Calculations of Results:
Once the lithium, calcium, and magnesium concentrations were known in all 34 shaker samples and in the “total” solution, the percent inhibition was calculated for each treatment. The lithium was used as a tracer of evaporation in each flask (typically about ten percent of the original volume). The lithium concentration found in the “total” solution was assumed to be the starting concentration in all 34 flasks. The concentrations of lithium in the 34 shaker samples were each divided by the lithium concentration found in the “total” sample. These results provided the multiplying factor for increases in concentration, due to evaporation. The calcium and magnesium concentrations found in the “total” solution were also assumed to be the starting concentrations in all 34 flasks. By multiplying these concentrations by each calculated evaporation factor for each shaker sample, the final intended calcium and magnesium concentration for each shaker sample was determined. By subtracting the calcium and magnesium concentrations of the “blank” from both the actual and intended concentrations of calcium and magnesium, then dividing the resulting actual concentration by the resulting intended concentration and multiplying by 100, the percent inhibition for each treated sample was calculated. The triplicate treatments were averaged to provide more accurate results.
Example:
“Total” concentration analysis results:
-
- Li=1.61 mg/L
- Ca=158.0 mg/L
- Mg=50.0 mg/L
“Blank” concentration analysis results:
-
- Li=1.78 mg/L
- Ca=4.1 mg/L
- Mg=49.1 mg/L
Shaker sample concentration analysis results:
-
- Li=1.78 mg/L
- Ca=150.0 mg/L
- Mg=54.0 mg/L
By taking the Li concentration from the shaker sample and dividing by the Li concentration in the “total” sample, the evaporation factor was determined as—
⇒1.78 mg/L/1.61 mg/L=1.11
By multiplying the Ca and Mg concentrations in the “total” sample by this factor, the final intended concentrations of Ca and Mg in the shaker sample were determined as—
Ca⇒1.11×158.0 mg/L=175.4 mg/L CaMg⇒1.11×50.0 mg/L=55.5 mg/L Mg
Finally, by subtracting the calcium and magnesium concentrations of the “blank” from both the actual and intended concentrations of calcium and magnesium, then dividing the resulting actual concentrations of Ca and Mg in the shaker sample by the resulting final intended concentrations and multiplying by 100, the percent threshold inhibition of calcium and magnesium was calculated as—
Ca⇒((150.0 mg/L−4.1 mg/L)/(175.4 mg/L−4.1 mg/L))×100=85.2% Ca inhibitionMg⇒((54.0 mg/L−49.1 mg/L)/(55.5 mg/L−49.1 mg/L))×100=76.6% Mg inhibition
The polymers of Example 7 and 8 were tested according to the procedure outlined above.
TABLE 8
percent calcium carbonate inhibition
%%%%
inhibitioninhibitioninhibitioninhibition
Polymerat 2 ppmat 3 ppmat 4 ppmat 5 ppm
Example 7618792
Example 88799100
Polymer of567594100
Example 7
without
fluorescent
tag
In the test above, anything above 80% inhibition is considered acceptable. These data in Table 8 indicate that the carbonate inhibition performance of the polymer is the same with the fluorescent tag as it is without the tag, indicating that the presence of the tag does not interfere with the primary purpose of the polymer which is scale minimization.
The specific examples herein disclosed are to be considered as being primarily illustrative. Various changes beyond those described will, no doubt, occur to those skilled in the art; and such changes are to be understood as forming a part of this invention insofar as they fall within the spirit and scope of the appended claims.