The present invention relates to cleaning of deposits or scale or fouling and in particular, to cleaning of deposits or scale or fouling from complex structures where there are difficulties in reaching to their parts.
Equipment performance can deteriorate over time as result of accumulation of dust, mud, rust, microorganisms, oil, scale and other deposits. Heat exchangers can lose their thermal efficiency that may result inadequate and sometimes dangerous thermal conditions, higher energy consumption and bottlenecks in production.
The propensity of water or steam or other solvents to form solutions and emulsions is used in various cleaning processes. Many industrial processes rely on using water or steam or other solvents to dissolve and extract substances, sometimes with chemicals that are dissolved or solids that are suspended in water or steam or other solvents. Yet, there are some problems associated with the use of water or steam or other solvents. Apart from equipment mechanical or chemical damage, there is a global water crisis that has become a major concern with humanitarian implications. Additional environmental difficulties relate to treatment and disposal of waste water that had become costlier, as result of increasing environmental concern and governmental regulatory pressures. The capital intensive investments in the construction and the operation of large water infrastructures and wastewater treatment plants involve sometimes funding and technologies that are unavailable in some regions.
Existing methods for industrial cleaning of open equipment involve in washing with high pressure water or steam, use of soap or detergents or foam, dry-ice or various chemicals; however there are some problems that are associated with the usage of those techniques: impact on human health and the environment, a need to shut down equipment, special arrangements required to facilitate access to unreachable parts, possible damage to equipment caused by: thermal shocks, abrasion, erosion, chemical attack and other damages that remain after the treatment such corrosion, scale, stress cracks.
There is a long time need for a technique that will overcome the above mentioned disadvantages and negative impacts of the existing art.
The present inventor has formed a way to avoid the shortcomings of the existing cleaning techniques by using waterless system allowing minimal shut down time, reduction equipment damage and environmental friendliness.
The present invention addresses a long time existing need for an efficient method for cleaning with minimum damage to equipment and infrastructure. The present invention is based on pneumatic spraying of dry thin powder. The system is designed to combine a chemical cleaning with a mechanical cleaning. In case of large scale facilities, the invention allows cleaning from bottom to top which obviates the need for special arrangements such as confined space entry, scaffolding and removal of safety nets in order to reach higher or internal parts. The synergetic effect of the combined mechanical and chemical cleaning facilitates an efficient removal of both organic and inorganic dirt. The chemical cleaning involves in a reaction of cleaning chemicals with the organic matter such as: oils, greases, hydrocarbons, cellulose. The mechanical cleaning involves a non-aggressive removal of inorganic matter such as dust, sand, mud and scale. Microorganisms are removed by chemical and mechanical cleaning.
The present inventor has found nontoxic, non-hazardous, environmental friendly usage of a mixture of sodium carbonate, sodium bicarbonate, sodium hydroxide and silicon dioxide (silica) achieves preferred results. Different ratios of those chemicals may be selected according to the specific structural material that should be cleaned and the conditions of which the cleaning process should be performed. For example, when there are structural materials that are sensitive to basic conditions, usage of sodium hydroxide shall be reduced or entirely eliminated. Using the above mentioned chemicals in thin powder form is to obviate the need to penetrate through finned tubes and clean residues after the treatment. In some rare cases of some small leftovers, their removal will involve only use of pressurized air to remove them.
a, b, c, d, e are schematic illustrations showing some structural features according to an aspect of the present invention related to equipment used to spray the cleaning mixture
The present inventor has found a way to avoid the shortcomings of the existing cleaning techniques by using waterless cleaning of equipment parts that are difficult to reach while the present invention is based on pneumatic spraying of dry thin powder. The cleaning process is a combination of chemical and mechanical cleaning. For large scale structures, the invention allows cleaning from bottom to top with no need for special arrangements such as confined space entries, scaffolding and removal of safety nets that are usually applied for maintenance activities at heights. The synergistic effect of combination of mechanical and chemical cleaning facilitates surprising efficient removal of both organic and inorganic dirt. The chemical cleaning involves in reactions of chemicals with organic matter such as oils, greases, hydrocarbons, cellulose. The mechanical cleaning involves in a non-aggressive removal of inorganic matter such as dust, sand, mud and scale. Microorganisms are removed by chemical and mechanical cleaning. The present invention addresses a long time existing need for an efficient method of cleaning with minimum damage to equipment and infrastructure.
The present inventor has found that preferred results can be achieved using a mixture of sodium carbonate, sodium bicarbonate, sodium hydroxide and silicone dioxide (silica) which are nor toxic or hazardous and are environmentally friendly. Different ratios among those chemicals can be selected according to the structural material that need to be cleaned and the conditions in which cleaning should be performed. For example, when there are structural materials that are sensitive to basic conditions, usage of sodium hydroxide will be reduced or entirely eliminated.
Using sodium bicarbonate is intended to moderate basic conditions caused by the sodium carbonate and sodium hydroxide, however, when cleaning surfaces that are contaminated with acidic scale, the cleaning mixture will contain less sodium bicarbonate and more sodium carbonate and sodium hydroxide. Sodium carbonate and sodium hydroxide are more basic than sodium bicarbonate. In addition, those two substances decompose at higher temperatures compared to sodium bicarbonate, however usually the cleaning mixture will contain also sodium bicarbonate in order to moderate too extreme basic conditions. Usage of sodium bicarbonate is also intended to moderate possible hazardous conditions when using higher concentrations of sodium hydroxide.
In high ambient humidity such as in rainy areas, up to 20% silica are being added to the cleaning mixture, while in dry climates, small quantities of silica are added if at all. The addition of pure silica may assist to avoid clogs in the spraying equipment caused by interactions between the humidity and the other ingredients in the cleaning mixture. The inventor had found that adding silica that has a relatively high molecular weight, (compared to water for example) contributed to the efficiency of the cleaning process and the flow of the cleaning mixture toward different parts of dense structure that is under cleaning process. In some cases, a mixture of pure or close to pure sodium bicarbonate is used, especially when moderate basic conditions are required.
As opposed to existing techniques, thin powder used in accordance with the present invention usually eliminates the need to remove leftovers. In rare cases that some residues remain, a limited use of pressurized air will be sufficient. Particle size of the thin powder used according to a preferred embodiment of the present invention shall be between 20-100 μm.
The below explanations concerning using the present invention to clean air-cooled heat exchangers also known as “fin-fan” air coolers or “fin-fans” heat exchangers, will reveal a possible application embodying the principles of the present invention.
Air coolers or “fin-fans” can be found in oil refineries, petrochemical or chemical plants, power plants, geothermal plants, nuclear plants and etc. On-line chemical cleaning of air cooled heat exchangers is applicable for flat type or “pagoda” or “A” type air coolers, whether they are horizontal or vertical, forced draft or induced draft.
The fin fan heat exchanger is designed to reject heat to the surrounding from a fluid or a gas flowing in finned tubes which increase the surface area and the heat removal rate. There are two well established low cost techniques for heat removal, using water or air as the coolant. The disadvantage of using water is related to the need in constructing and maintaining infrastructure for transfer of the water from a reservoir to the heat exchanger and back to the reservoir, and the need to cool the water and treat them before recirculating them. In some cases, water can be in scarce and the reservoir can be remote. In addition, there is a need to treat the water with chemicals and with filtration, but in order to avoid accumulation of sediments and chemicals some of the water are excreted out, thus endanger the environment. The public awareness for water shortage and for the need to protect the environment is increasing and so, also difficulties, costs and regulations that are associated with treatment and disposal of wastewater. Using air-cooled heat exchangers minimizes those mentioned concerns. An air-cooled “fin-fan” heat exchanger can be as small as car radiator or large enough to cover several acres of land, as is the case on air coolers for large power plants.
“Fin fans” are constructed of finned tubes that are arranged in bundles with very limited space between them. Typically, each bundle is constructed from 4 to 12 layers of finned tubes, the fins are usually made of aluminum or copper with high heat transfer coefficients. Over time, the thin fins and the gaps between tubes may accumulate dust, mud, sand, hardened calcium carbonate, organic materials like oil or polymers, and other deposits that significantly reduce the thermal efficiency of the heat exchanger, resulting higher process outlet temperatures; high energy consumptions and production bottlenecks.
Common existing techniques for cleaning fin fan bundles are: washing with high pressure water, using soaps, detergents or foam, dry-ice (which is solid CO2) or chemicals such as weak citric acid. For applying those techniques, long periods of equipment shutdowns are required, dealing with large quantities of residues after the cleaning and difficulties in reaching all parts of the heat exchanger, (such as elevated parts). In addition, the existing techniques cause damage to equipment some of which may be sensitive to water, for example heat exchanger control instruments, electric motors, etc.
The present invention is intended to overcome the above mentioned and further drawbacks of the existing art, as described in the below listing:
The cleaning a “fin-fan” heat exchanger, according to one aspect of the present invention comprises the below equipment:
In a preferred embodiment of the invention, compressed air is supplied in a minimum rate of 400 CFM at a range of 75 to 180 psi. Accordingly, the modified blasting machine operates under maximum pressure of 180 psi and the spraying hoses are rated for 180 psi.
Applying the present invention for cleaning of “fin-fan” air coolers facilitates an increase in the thermal efficiency of the heat exchanger, while reducing outlet process temperatures, lowering energy consumption increasing production rate and better environmental protection.
Hereunder few examples of using an aspect of the present invention for cleaning of “fin-fan” air coolers:
Cleaning of “fin-fan” air coolers in a refinery in Argentina that were contaminated by spills of acidic hydrocarbons, mostly light kerosene and naphtha which contain high percentage of sulfur. The sulfur, together with water vapor from the air, creates sulfuric acid which is very corrosive. A mixture which contained 60% Sodium Carbonate, 20% sodium hydroxide and 20% sodium bicarbonate was used in order to simultaneously clean and neutralize the acidic contamination.
Cleaning of “fin-fan” air coolers in a petrochemical plant in Canada. The air coolers were contaminated with dust, mud and sand, which are mostly chemically inert components. A mixture which contained 90% sodium bicarbonate and 10% sodium carbonate, because there was no need to neutralize acidity.
Cleaning of “fin-fan” air coolers in a chemical plant for production of Ammonia in Texas where the air coolers were contaminated with some unspecified acidic material in a very humid tropical environment. The cleaning mixture contained 40% Sodium Carbonate, 50% Sodium Bicarbonate and 10% of silica. This mixture allowed free flowing of strong alkali stream to neutralize the acidic material. Also, an air-dryer and a water separator were in use, located between the air compressor and the blasting machine, due to the high humidity.
Number | Date | Country | |
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62197015 | Jul 2015 | US |
Number | Date | Country | |
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Parent | 15215308 | Jul 2016 | US |
Child | 15947149 | US |