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Product Code: RXSOL-44-6299-030
Sodium Molybdate 35% manufacturer supplier distributor in Mumbai, Kandla, Kolkata, Vizag, Chennai, India, Fujairah, Dubai, Sharjah, UAE, Gulf, Middle East, Muscat Oman, Kenya Africa. Get the best quality of Sodium Molybdate 35% at a competitive price from us. We have ready stock of Sodium Molybdate 35% in India, UAE Gulf, Oman, Kenya Africa. Contact us for bulk as well as small orders.
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-44-6164-025
leading Indian Manufacturers of Sodium Molybdate, Ammonium Molybdate and Molybdenum Trioxide.
Sodium Molybdate is Roasted Molybdenum oxide/Canada/USA/ Belgium.
Our other valuable molybednum product list is as follows :::
All the above products are available in different grades like AR/LR/ACS/TECHNICAL with different purity levels and concentrations.
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Sodium Molybdate supplier in Mumbai, Gandhidham, Fujairah, Chennai, Dubai, Kolkata, Abudhabi, Navi Mumbai MIDC, Ajman, Visakhapatnam, Sharjah. We are most popular sodium molybdate supplier in India as well as in Middle East.
Feel free to ask for small packing LR grade of sodium Molybdate as well as technical grade of Sodium molybdate in Large Packing.
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-40-4023-020
Corrosion Inhibitor Nitrite Borax based for cooling water circulation system manufacturer and supplier in Dubai, Nairobi, Mombasa, Kenya, Uganda, Mumbai, Kolkata, Visakhapatnam, Chennai, Haldai, Ennore, Paradip, Gandhidham, Surat, Canada, Dubai, Sharjah, Ajman, Abudhabi, UAE Middle East, Sohar Barka Muscat Oman
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-40-4043-220
Pennstopsol 85 (Corrosion Inhibitor) manufacturer supplier distributor in Mumbai, Kandla, Kolkata, Vizag, Chennai, India, Fujairah, Dubai UAE, Muscat Oman, Kenya Africa. Get the best quality of Pennstopsol 85 (Corrosion Inhibitor) at a competitive price from us. We have ready stock of Pennstopsol 85 (Corrosion Inhibitor) in India, UAE Gulf, Oman, Kenya Africa. Contact us for bulk as well as small orders.
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-19-1503-210
Acids and corrosive materials are used to enhance production and to stimulate reservoirs therefore special care is required to ensure that casing, tubing strings and downhole equipment are not damaged. Blend of ACID with Acid corrosion Inhibitor RXSOL 213 protect your downhole equipment and metal tubulars.
Exhibits excellent sequestration of metal ions and threshold inhibition of metal salt precipitation. Its hydrolytic stability makes it a versatile ingredient for applications requiring efficient metal ion control. Acid corrosion Inhibitor RXSOL 213 excellent scale and corrosion inhibition and good thermal tolerance ability.
Acid Corrosion inhibitor manufacturer. exporter and supplier in India Kuwait, UAE, Oman, Mumbai Maharastra, Chennai Tamilnadu, Kolkata WestBengal, Visakhapatnam Andhrapradesh, Gandhidham Surat Gujrat, Fujairah Dubai Sharjah Ajman Abudhabi, Oman Muscat Sohar, Canada, Nairobi Kenya Africa
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-16-2065-210
H2S Scavengers and Speaciality Chemicals to Reduce Hydrogen Sulfide Exposure
Harmful and Colorless toxic gas, Toxic Odor like rotten egg in to the working environment is due to presence of good amount of Hydrogen Sulfide in the system.
Hydrogen Sulfide is corrosive and Acidic GAS towards metal equipment practically observed that within 5 years can cause millions of dollars in damage to infrastructure.
RX Marine International offers a compleate line of water soluble and oil soluble hydrogen sulfide scavengers that can be applied via continous injection or through batch treatments.
HS Code : 3811900
HYDROGEN SULFIDE SCAVANGER
MMA Triazine is a cyclic tertiary triamine. It is mainly used as a scavenger for sour gases like H2S and mercaptans in gaseous or liquid hydrocarbon streams
The MMA-triazine reacts with H2S or mercaptan resulting in the formation of dithiazines. Both MMA-triazine and its reaction products are readily biodegradable.
MMA-triazine is available as an aqueous solution with concentration up to 42%.
KEY Feature
• Can be applied in both aqueous and hydrocarbon streams
• Effective removal of H2S down to ppm levels
• Product and its reaction products are readily biodegradable
Carbon Dioxide and H2S Corrosion Inhibitor manufacturer and supplier in Mumbai, Kandla, Chennai, Visakhapatnam, Kolkata, Dubai, Fujairah, Sharjah, Abudhabi, Muscat, Sohar, Barka RUWI, Oman, Nairobi Kenya Africa, Canada
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-16-1047-025
Before handling the chemical products used in this process, the first aid and handling recommendations on the Material Safety Data Sheet for should be read, understood and followed. The industrial cleaning bath is strongly acid and can burn skin and eyes. Refer to the Material Safety Data Sheet for hydrochloric acid for recommendations for protective action.
Acid corrosion Inhibitor RXSOL-16-1047-025 manufacturer and supplier in Mumbai, Surat, Gandhidham - Kandla, Surat, Gujrat, Kudra Bihar, Chennai - Ennore, Visakhapatnam - Gangavaram, Kolkata - Haldia, Fujairah - Dubai - Sharjah Middle East UAE, Muscat, Sohar, Oman, Varanashi UP India
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-16-2069-210
Corrosion Inhibitor for Gas Compressor are efficient corrosion inhibitors developped to protect oil and gas production installations against internal corrosion. This includes protection of water systems specific to oil fields (produced water disposal systems and production, treatment and injection waters facilities). Corrosion Inhibitor for Gas Compressor offers an optimum corrosion inhibition whatever the fluid characteristics and field conditions: CO2 and/or H2S p
Corrosion Inhibitor for Gas Compressor manufacturer supplier distributor in Mumbai, Kandla, Kolkata, Vizag, Chennai, India, Fujairah, Dubai UAE, Muscat Oman, Kenya Africa. Get the best quality of Corrosion Inhibitor for Gas Compressor at a competitive price from us. We have ready stock of Corrosion Inhibitor for Gas Compressor in India, UAE Gulf, Oman, Kenya Africa. Contact us for bulk as well as small orders.
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-16-1047-210
Corrosion inhibitor especially designed to inhibit the attack of hydrochloric acid on iron and steel during industrial cleaning operations. It also inhibits acid attack on copper and brass. It does not contain arsenic, chlorinated hydrocarbons, or lead compounds.
Corrosion Inhibitor manufacturer and supplier in Mumbai, Gandhidham, Vizag - Visakhapatnam, Chennai, Kolkata, Fujairah, Dubai, Sharjah, Ajman, Abudhabi, Muscat - Oman.
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.
Product Code: RXSOL-40-4035-025
Risk of serious damage to eyes. In case of contact with eyes, rinse immediately with plenty of water & seek medical advice. Wear suitable gloves and eye / face protection
Pipeline corrosion inhibitor manufacturer and supplier. RXSOL 4000 provide complete protection against rust and scale.
Pipe Line and Tank Hydro Testing Corrosion Inhibitor RXSOL 4000 is Hydro-testing corrosion protection for Pipeline, Tank. RXSOL 4000 Chemical for conditioning of hydro test water i.e. blend of corrosion inhibitor, one Oxygen scavenger, one scale inhibitor & one biocide manufacturer exporter and supplier Mumbai, Surat, Gandhidham, Chennai, Ennore, Visakhapatnam, Kolkata, Haldia, Paradip, Fujairah, Sharjah, Ajman, Abudhabi, Dubai UAE Middle East, Muscat Oman Sohar, Canada
DESCRIPTION :
RXSOL 4000 is a multicomponent, multifunctional formulation which prevents corrosion, microbiological growth in single product treatment programme.
PERFORMANCE:
CORROSION: Effectively prevents corrosion due to Carbon Dioxide, inorganic salts, dissolved oxygen & Hydrogen sulphide contamination from sour fluid or bacterial action. The inhibitor acts as a cathodic polarizer.
MICROBIOLOGICAL GROWTH: Effectively prevents the metabolic function necessary for reproduction of the bacteria cell. Successfully prevents anaerobic/aerobic and sulphate reducing bacteria.
APPLICATION :
Inhibitor, corrosion, multicomponent, multifunctional: For prevention of corrosion and microbiological growth in water flood systems during hydrostatic testing and other applications
DOSE :
RXSOL 4000 can be fed directly or through chemical doses pump. Doses may vary with the quality of water to be treated and the residence time of the water in the system.
DOSING RATE OF RXSOL 4000
Minimum 50 LPH
Maximum 125 LPH
Actual dosing rate shall be proportionate to pumping rate.
Flow Rate Of The Product
Minimum M3/ HR : 150.0
Maximum M3/ HR : 350.0
Location for dosing of RXSOL 4000 corrosion inhibitor chemical
# Corrosion inhibitor shall be dosed in the displacement water piping at the suction of main pump/ booster pump
For Storage tank it can dose 0.50 to 0.15 Ltr per 100 Ltr Water.
CHEMICAL SPECIFICATION :
| Form | Liquid |
| Colour | Colourless to slightly Yellow |
| Odour | Sharp |
| Flash Point | > 100C |
| Density | 1.05-1.11 g/cm3 (25C) |
| pH | 3 - 7 |
Benefit / Advantage :
TECHNICAL DATA SHEET
CORROSION PROBLEMS DURINGHYDROTESTING OF PIPELINES
The major factor which contributes to the corrosion in hydro-static test water is the dissolved oxygen and dissolved solids do not have much impact on the corrosion rate except the chloride content. The presumptions like not using the corrosion inhibitor if the water is not with high mineral content could beM disastrous as in fact any corrosion process, even a very mild one, will be accompanied by the set up of galvanic cells and formation of corrosion products deposits. Such environment makes the conditions ideal for the corrosion process to continue at accelerated rate once the process fluid will be run through the line.
Effect of Dissolved Oxygen:
Dissolved oxygen plays a key role in corrosion or iron in natural waters, but its effects can be conflicting and partially dependent on other environmental factors. In near neutral pH waters at ambient temperature, dissolved oxygen provides the reduction reaction which sustains the corrosion of iron. However, oxygen also plays a role in formation of semi-protective iron oxide films on the metal, and the more protective films are formed at higher oxygen concentrations. Once these films are formed, however, oxygen provides the main driving force for initiation of pitting (leading to tuberculation) or other forms of localized corrosion. The first part of this discussion is for conditions in the absence of calcium carbonate or other external inhibiting species.
At sufficiently high pH values, iron oxide or hydroxide layers can be formed. The first of these is probably ferrous hydroxide which can be formed by an overall reaction such as
Fe + H2O + 1/2 O2 = Fe (OH)2
This solid is often found next to the metal surface and can act as a diffusion barrier to oxygen. Further oxidation of this product yields hydrous ferric oxide which comprises most of ordinary rust. An intermediate oxidation stage, Fe3O4. nH2O often forms as a layer between the ferric and ferrous compounds. In the absence of dissolved oxygen, the corrosion rates for both pure iron and steel becomes negligible in near neutral pH water at room temperature.
Corrosion rates may be high when the metal is first exposed to air-saturated water, but the iron oxide films formed over a period of a few days act as a barrier to diffusion of oxygen to the surface and a steady state corrosion rate is obtained. This steady state rate is proportional to oxygen concentration, since the oxygen diffusion rate is proportional to its concentration.
An oxygen concentration of about 6 mg/l corresponds to air-saturated water. At still higher oxygen concentrations, the uniform corrosion rate of mild steel may decrease abruptly. This effect is apparently due to passivation of the iron which involves either the oxidation of the normal ferrous hydroxide layerto one which has better protective properties or the formation of a thin chemisorbed oxygen layer on the metal surface. More oxygen is required in waters containing chloride ions and passivation of mild steel cannot occur if the chloride concentration is high enough. The breakdown of passivity in the presence of moderate amounts of chlorides (more than about 20 ppm, see below) is often accompanied by severe pitting or crevice corrosion. The effect of solution flow rate on mass transport of oxygen to the corroding surface can also give rise to diverse effects. At moderate oxygen concentrations and flow rates, increasing the flow rates increases the corrosion rate due to the increase in amount of oxygen transported to the surface. At higher flow rates, the surface oxygen concentration can become high enough to cause passivation, provided the chloride content is not too high. Still higher flow rates, over 4.0 M/sec, can greatly accelerate corrosion by erosion of the protective films, combined with fast transport of oxygen to the surface by turbulent flow. At the other extreme, stagnant conditions are usually
most conducive to pitting and other forms of localized corrosion. The threshold for chloride effects on passivity is ill defined. As little as 20 ppm. Chloride may cause breakdown and pitting but the threshold may be higher depending on solution composition.
Effect of Dissolved Salts:
Dissolved salts (for example, ions such as Na+, Cl- , SO42-, Ca2+ , Mg2+, HCO3, CO32-can have a number of effects, some of which depend only on the general effect of ions, whileothers depend on the individual chemical species. Examples of the first class of effects are given below.
Increasing salt concentration increases solution conductivity which can have several effects.
Increasing salt concentration generally decreases the equilibrium concentration of dissolved oxygen and CO2
Contrary to early predilections, solution conductivity itself has little effect on most modes of uniform or localized corrosion. This is because the local anodes and cathodes are so close together that the resistance offered by the solution is much less than equivalent electrochemical reaction rate resistance. Solution conductivity can, however, affect the range over which the effects of attack due to galvanic coupling of dissimilar metals is extended. Attack can extend for example, from about 1 cm. from the joint in soft waters to more than 10 cm. in water with significant dissolved salt content. Changes in solution conductivity can have more subtle and significant effects. It has been proposed that moderate increases in conductivity (by dissolved NaCl) from that of very soft or distilled water can lead to increased corrosion rates due to formation of a less protective Fe (OH)2 film. The film is less protective since it is formed further away from the surface than in less conductive waters. This in turn is due to coupling of local anodic (source of Fe 2+) and cathodic (source of OH-) areas at greater distances in the more conductive solution. The initial increase in corrosion rate might also have to do with some specific effects of chloride and a number of postulates on these effects have been offered. Specific effects of chloride are discussed below.
There is little direct evidence for either the Fe (OH)2 film or chloride effect arguments. It has recently been proposed that an increase in solution con-ductivity may have the effect of actually promoting a more protective coating on iron in the presence of Calcium Carbonate film forming precursors. Correlation between the electrical impedance and protectiveness of scales and a quantity related to the conductivity of the solution was found. Conductive salts facilitate protective film formation, provided that sufficient temporary hardness exists.
The other overall effect of dissolved salts that of decreasing the solubility of dissolved gases. Since the dissolved oxygen content is the main controlling factor under the conditions, "salting out" of oxygen causes a decrease in corrosion rate.
Technical Notes
This effect only becomes pronounced at higher salt concentrations and is most likely unimportant in natural fresh waters. Chloride is the most deleterious individual ionic species normally occurring in natural waters. Much of this appears to be due to the ability of chloride to promote pitting by penetration or local destruction of otherwise protective iron oxide films. It is quite difficult for a uniform, true passive iron oxide film to be formed in the presence of chloride ions. It is difficult, however, to quantify the relation of corrosivity to chloride concentration in natural waters. The threshold concentration of chloride above which pitting of iron is possible, is said to be About 10 ppm. The role of sulfate is more nebulous, especially since sulfate does not appear to have the film piercing properties that chloride displays.
The corrosivity of air-saturated domestic waters depends on the following factors
.
The proportion of corrosive agents (chloride and sulfate ions) to inhibitive agents (bicarbonate, carbonate, hydroxide, and calcium ions).
The concentration and degree of effectiveness of the corrosive and inhibitive species.
The velocity of flow which affects the rates of diffusion of both types of species to the surface.
The relative effectiveness of the species involved is not definitive, but may be influenced by one or more of the others. The interdependence of the relevant factors is also emphasized by the observation that "intermediate proportions" of corrosive to inhibitive species, which result in incomplete protection (to uniform corrosion) at a particular solution flow rate, are conducive to pitting and/or tuberculation.
Effect of Micro – Organisms:
All water used for Hydro-testing generally contains iron bacteria and sulphate reducing bacteria. The iron bacteria attack to the pipe wall mostly at 6 o’clock location and produces tubercle of iron oxide by metabolic action. Below the tubercles, sulphate reducing bacteria grows and generates H2S from sulphate of water. The H2S goes on reacting with iron forming Fe2S. This is combined with auto catalytic formation of HCI under tubercle and lead to deep pitting and perforation of the pipe wall. The mechanism is more pronounced under stagnant condition and is relevant of Hydrostatic testing.
Oman, Bahrain, Abu Dhabi, Ajman, Al Ain, Dubai, Ras Al-Khaimah, Fujairah, Sharjah, Umm Al Quwain, Ruwais, Mina Zayed, Khalifa Port, Kizad, Jebel Ali, Port Rashid, Khor Fakkan, Sharjah Creek, Port of Hamriyah, Mussafah Port, Saqr Port, Dibba Port, Jebel Dhanna, Mina Al Hamriya, and all major UAE ports.