Buffer Cleaner
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PHYSICAL PROPERTIES INFORMATION
Physical state: Liquid
Color: Clear colorless liquid
Odor: Odorless pH: 2.2 (0.1 N sol)
Specific Gravity: 1.24 – 1.26
STORAGE INFORMATION Keep container(s) tightly closed. Store this material in cool, dry, well ventilated areas. Protect container(s) against physical damage. Containers of this material may be hazardous when empty since they retain product residues (vapors, liquid). Shelf life: Stored under controlled conditions 1 year.
Features and Benefits
Sodium Meta Bisulphite manufacturer in India, UAE, Canada, Best quality Sodium Meta Bisulphite SMBS ready stock in Mumbai, Kandla, Surat, Howrah, Vishakhapatnam, Chennai, Fujairah, Muscat Barka Oman, Kenya.
Importers of Trichloroisocyanuric Acid 90% China (TCCA), Sodium PerCarbonate Coated China Granules & Tablets, Potassium BiCarbonate China Extra Pure 99.9%, Sodium MetaBiSulphite China(SMBS), Sodium Silico Fluoride Taiwan"
Other names:Sodium hyposulfite, Hyposulphite of soda
Identifiers CAS number : 7772-98-7 Y, 10102-17-7 : (pentahydrate)
UNII :L0IYT1O31N Y
ChEMBL CHEMBL : 1201157 N
RTECS number :XN6476000
Molecular Formula |
Na2S2O3.5H2O |
Molar Mass |
158.11 g/mol |
Appearance |
Clear Liq |
Odor |
Odorless |
Density |
1.667 g/cm3 |
Melting Point |
48.3 °C (pentahydrate) |
Boiling Point |
100 °C (pentahydrate, - 5H2O decomp) |
Solubility in Water |
76.4 g/100 g H20(20 °C) |
IUPAC name :Sodium thiosulfate
Other names:Sodium hyposulfite ,Hyposulphite of soda
Identifiers
CAS number : 7772-98-7 Y,
10102-17-7 : (pentahydrate)
PubChem: 24477
ChemSpider :22885 Y
UNII :L0IYT1O31N Y
ChEMBL CHEMBL : 1201157 N
RTECS number :XN6476000
Keep away from heat as the potential for release of sulfur dioxide fumes exists. Liquid sodium thiosulfate has very low toxicity but routine safety precautions should be practiced. Rubber gloves, safety goggles and protective clothing is recommended.
Sodium Thiosulfate, wt%30 +/- 2%
Sulfite, wt%1.5 max.
pH 7.0 – 9.0
Physical Properties:
Specific Gravity @ 25o C 1.252 – 1.34
Density, lbs/gal @ 25o C 10.4 – 11.2
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Oxygen Control
Chemical Oxygen Scavengers. The oxygen scavengers most commonly used in boiler systems are sodium sulfite, sodium bisulfite, hydrazine, catalyzed versions of the sulfites and hydrazine, and organic oxygen scavengers, such as hydroquinone and ascorbate.
It is of critical importance to select and properly use the best chemical oxygen scavenger for a given system. Major factors that determine the best oxygen scavenger for a particular application include reaction speed, residence time in the system, operating temperature and pressure, and feedwater pH. Interferences with the scavenger/oxygen reaction, decomposition products, and reactions with metals in the system are also important factors. Other contributing factors include the use of feedwater for attemperation, the presence of economizers in the system, and the end use of the steam. Chemical oxygen scavengers should be fed to allow ample time for the scavenger/oxygen reaction to occur. The deaerator storage system and the feedwater storage tank are commonly used feed points.
In boilers operating below 1,000 psig, sodium sulfite and a concentrated liquid solution of catalyzed sodium bisulfite are the most commonly used materials for chemical deaeration due to low cost and ease of handling and testing. The oxygen scavenging property of sodium sulfite is illustrated by the following reaction:
2Na2SO3 | + | O2 | ® | 2Na2SO4 |
sodium sulfite | oxygen | sodium sulfate |
Theoretically, 7.88 ppm of chemically pure sodium sulfite is required to remove 1.0 ppm of dissolved oxygen. However, due to the use of technical grades of sodium sulfite, combined with handling and blowdown losses during normal plant operation, approximately 10 lb of sodium sulfite per pound of oxygen is usually required. The concentration of excess sulfite maintained in the feedwater or boiler water also affects the sulfite requirement.
Sodium sulfite must be fed continuously for maximum oxygen removal. Usually, the most suitable point of application is the drop leg between the deaerator and the storage compartment. Where hot process softeners are followed by hot zeolite units, an additional feed is recommended at the filter effluent of the hot process units (prior to the zeolite softeners) to protect the ion exchange resin and softener shells.
As with any oxygen scavenging reaction, many factors affect the speed of the sulfite-oxygen reaction. These factors include temperature, pH, initial concentration of oxygen scavenger, initial concentration of dissolved oxygen, and catalytic or inhibiting effects. The most important factor is temperature. As temperature increases, reaction time decreases; in general, every 18°F increase in temperature doubles reaction speed. At temperatures of 212°F and above, the reaction is rapid. Overfeed of sodium sulfite also increases reaction rate. The reaction proceeds most rapidly at pH values in the range of 8.5-10.0.
The following operational conditions necessitate the use of catalyzed sodium sulfite:
High feedwater sulfite residuals and pH values above 8.5 should be maintained in the feedwater to help protect the economizer from oxygen attack.
Some natural waters contain materials that can inhibit the oxygen/sulfite reaction. For example, trace organic materials in a surface supply used for makeup water can reduce speed of scavenger/oxygen reaction time. The same problem can occur where contaminated condensate is used as a portion of the boiler feedwater. The organic materials complex metals (natural or formulated catalysts) and prevent them from increasing the rate of reaction.
Sodium sulfite must be fed where it will not contaminate feedwater to be used for attemporation or desuperheating. This prevents the addition of solids to the steam.
At operating pressures of 1,000 psig and higher, hydrazine or organic oxygen scavengers are normally used in place of sulfite. In these applications, the increased dissolved solids contributed by sodium sulfate (the product of the sodium sulfite-oxygen reaction) can become a significant problem. Also, sulfite decomposes in high-pressure boilers to form sulfur dioxide (SO2) and hydrogen sulfide (H2S). Both of these gases can cause corrosion in the return condensate system and have been reported to contribute to stress corrosion cracking in turbines. Hydrazine has been used for years as an oxygen scave
Sodium Meta Bisulphite manufacturer in India, UAE, Canada, Best quality Sodium Meta Bisulphite SMBS ready stock in Mumbai, Kandla, Surat, Howrah, Vishakhapatnam, Chennai, Fujairah, Muscat Barka Oman, Kenya.
Importers of Trichloroisocyanuric Acid 90% China (TCCA), Sodium PerCarbonate Coated China Granules & Tablets, Potassium BiCarbonate China Extra Pure 99.9%, Sodium MetaBiSulphite China(SMBS), Sodium Silico Fluoride Taiwan"
Formula | NaHSO3 |
Molecular Weight | 104 |
Sodium Bisulfite, wt% (Na2S2O5) | 38.0 - 42.0 |
Sodium Sulfate, wt% | ≤ 3.5% |
Solubility (10 % Aquous Soln) | V. S. Hazy to clear solution. |
pH Value of 5% Solution | 3.5 to 4.5 |
Specific Gravity @ 25° C | 1.310 – 1.370 |
Density, lbs/gal @ 25° C | 10.9 - 11.3 |
Description | Sodium Bisulfite 40% Solution (NaHSO3) is a pale yellow liquid. |
Standard Packing | 50 Kg. / 250 kg HM HDPE Barrel |
Appearance | White Powder, Granular, |
Chemical Name | Sodium Dichloroisocyanurate |
Formula | C3O3N3Cl2Na |
Chlorine | >62% |
Molecular Weight | 219.95 |
pH (1% solution) | 6.0 to 7.0 |
Moisture | 0.5 to 1.00% max |
Solubility @ 25°C | Completely soluble in water |
Density | Tap density = 0.974 g/mL |
The requirements for pool water testing in the application of dichlor based products should be indicated on the product label. The primary parameter to be tested is the level of FAC in the water. The choice of testing methods will vary depending on the type of pool (residential or commercial) and local regulations and standards. The product label should recommend that the pool water quality be properly balanced. This requires testing of the pool water balance parameters of pH, alkalinity, calcium hardness, and stabilizer (i.e. cyanuric acid).