WO2014193230A1

WO2014193230A1 - Cooling water

Info

Publication number: WO2014193230A1
Application number: PCT/NL2014/050341
Authority: WO
Inventors: Edwin Matheus FOEKEMA
Original assignee: Stichting Dienst Landbouwkundig Onderzoek
Priority date: 2013-05-29
Filing date: 2014-05-28
Publication date: 2014-12-04
Also published as: NL2010885C2; EP3003990A1

Abstract

The invention relates to environmentally friendly methods of reducing and/or preventing fouling on a surface of a component that is in contact with water. The invention further relates to a cooling system that is suited for employing the methods of the invention, and to a power plant, comprising such cooling system.

Description

l

Title: COOling water

Field: The invention relates to methods and means of reducing and/or preventing fouling on a surface of a component that is in contact with water.

Introduction

Thermoelectric power plants boil water to create steam, which then spins turbines to generate electricity. The heat used to produce steam can come from burning of a fuel, from nuclear reactions, or directly from the sun or geothermal heat sources underground. Once steam has passed through a turbine, it must be cooled before it can be reused to produce more electricity. This cooling of the primary water circuit is generally achieved by a separate cooling water system that consists of a condenser, a cooling tower, and a cooling water pump. The cooling water is either extracted from a nearby water source and discharged back into this source, or cooled down and recirculated for reuse as cooling water after cooling of the primary water circuit.

A first cooling system is also termed a once-through system. Such system takes water from a nearby source (e.g., river, lake, or ocean), circulates it through pipes to absorb heat from the steam in systems called condensers, and discharges the now warmer water to the local source. Once-through systems were initially the most popular because of their simplicity, low cost, and the possibility of situating power plants in places with abundant supplies of cooling water. A second cooling system is a closed-loop system, also termed a wet-recirculating system. Such system reuses cooling water in a second cycle rather than

immediately discharging it back to the original water source. Most commonly, wet-recirculating systems use cooling towers to expose water to ambient air. Some of the water evaporates; the rest is then returned to the condenser in the power plant. Because wet-recirculating systems only withdraw water to replace any water that is lost through evaporation in the cooling tower, these systems have much lower water withdrawals than once-through systems. Fouling of a water system, for example a cooling water system, is a major problem for the industry, for example for power plants. Methods for reducing fouling include the addition of a biocide such as, for example, chlorine to the water. However, chlorination is associated with high costs and environmental concerns due to the generation of chloromethanes and other organochlorines as by-products. Most countries, including European countries, have introduced measures to reduce the discharge of organochlorines into the aquatic

environment. Because of these measures, alternative chemical products, such as peracetic acid, are replacing chlorine. However, there is still a need for a more environmentally-friendly and cheap agent that prevents fouling on the surface of a water system.

Therefore, the invention provides a method of reducing and/or preventing fouhng on a surface of a component that is in contact with water, the method comprising: transferring carbon dioxide to the water to bring the water at a pH of at most 7.5, whereby the water is not pressurized. Said water preferably is fresh water, for example fresh cooling water that is used in a power plant.

The term "fresh water" includes surface water such as sea water, brackish water, river water, lake water, and ground water. Said water preferably is salt water, preferably seawater.

Fouling is the accumulation of unwanted material on solid surfaces to the detriment of function. Fouling is distinguished from other surface-growth phenomena in that it occurs on a surface of a component, system or plant performing a defined and useful function, and that the fouling process impedes or interferes with this function. The fouling material can consist of either living organisms (biofouling) or non-living substances including, for example, scaling. Biofouling is the accumulation of micro-organisms (e.g. algae and diatoms), plants, and animals on surfaces. Bacteria can form biofilms or slime layers. The organisms aggregate on surfaces using colloidal hydrogels of water and extracellular polymeric substances such as polysaccharides, lipids, and nucleic acids. Amongst the larger animals that cause widespread fouling are zebra mussel in freshwater, and blue mussel and oyster in seawater. Scaling, or precipitation fouling, is the undesirable accumulation of solid salts, oxides and hydroxides from water. These include, for example, calcium carbonate and calcium sulfate. Scale deposits are formed by precipitation and crystal growth at a surface in contact with water. The most common scale-forming salts that deposit on heat transfer surfaces are those that exhibit retrograde solubility with temperature. Although they may be completely soluble in the lower- temperature bulk water, these compounds (e.g., calcium carbonate, calcium phosphate, and magnesium silicate) supersaturate in the higher-temperature water adjacent to the heat transfer surface and precipitate on the surface.

Metallic surfaces are ideal sites for crystal nucleation because of their rough surfaces and the low velocities adjacent to the surface. Corrosion cells on the metal surface produce areas of high pH, which promote the precipitation of many cooling water salts. Once formed, scale deposits initiate additional nucleation, and crystal growth proceeds at an accelerated rate. The addition of carbon dioxide to water to prevent biofouling is known from United States Patent 6,821,442. As described herein, carbon dioxide is

transferred to water to supersaturate the water with dissolved carbon dioxide such that aquatic species are killed. For this supersaturation, the water is contained within a closed system and pressurized such that delta P is greater than 0.0 mm Hg. Delta P is calculated as:

Delta P = pN₂ + pO₂ + pH₂O + pCO₂ - pAtm, whereby pN₂ includes argon and other trace atmospheric gasses.

It is noted in US6,821,442 that supersaturation of water with carbon dioxide would induce gas bubble trauma (GBT), which may result in the killing of aquatic species. The present inventor now established that the transfer of carbon dioxide to water at a level such that delta P is below atmospheric pressure prevents growth of young shellfish, prevents scaling and results in distraction of fish. Surprisingly, the inventor established that transfer of carbon dioxide to a level such that the pH of the water is at most 7.5, is sufficient for prevention, or at least for reduction, of fouling on a surface of a component that is in contact with said water. The transfer of carbon dioxide to water at a level such that the pH of the water is at most 7.5, provides an environmentally-friendly and cheap agent to prevent fouling on the surface of a cooling water system. Carbon dioxide is a natural gas essential for life. Within the limits that are sufficient to reduce fouling, the elevated concentrations of carbon dioxide and consequently reduced pH levels will not result in acute killing of aquatic species, but will rather reduce propagation and reproduction. Said carbon dioxide is preferably transferred at an intake point of the water. Said water preferably is fresh water, including surface water such as sea water, river water and lake water, and ground water. Said fresh water preferably is salt water, preferably seawater. The pH of the water is preferably reduced to a pH of between 6.0 and 7.5, such as to a pH of 6.0, 6.1, 6.2, 6.3, 6.4, 6.5, 6.6, 6.7, 6.8, 6.9, 6.95, 7.0, 7.1, 7.2, 7.3 7.4 or 7.5. The pH is preferably not below 6, more preferably not below 6.5 in order not to cause damage to the water system such as corrosion of metal components. The pH of the water is therefore preferably between 6.5 and 7.5, such as 6.5, 6.6, 6.7, 6.8, 6.9, 6.95, 7.0, 7.1, 7.2, 7.3 7.4 or 7.5.

Sea water has, on average, a pH of about 8.5. To reduce the pH of sea water to a level of about 7.5, about 10 mgram of C02 is required per liter of water. To reduce the pH of sea water to a level of about 6.0, about 150 mgram of C02 is required per liter of water. Hence, the amount of C02 that is required per liter of water to adjust the pH of the water to a value of between 6.0 and 7.5 is between 10 and 150 mgram. This amount of C02 can be transferred to water using methods and means that are known in the art.

A pH of at most 7.5 will increase carbonate solubility and in this way effectively prevent shell fish such as cockles, mussels, and oysters, and other mollusc larvae from forming the shells necessary to settle and survive in the water system. In addition, the increased carbonate solubility of the water results in decreased scaling, while the increased carbon dioxide concentration results in deterrence of fish.

To reduce the pH of the cooling water of a plant that consumes about 213.120 m³/hr of cooling water to a pH of about 7 requires the addition of about 2771 kg/hr of CO2. To reduce the pH of the cooling water of a plant that consumes about 213.120 m³/hr of cooling water to a pH of about 6 requires the addition of about 29411 kg/hr of CO2. An example of such plant is the Amer power plant in Geertruidenberg, the Netherlands, which has a capacity of about 1245

megawatts. It is further preferred that the carbon dioxide that is transferred to the water to bring the water at a pH of at most 7.5, is produced by the industrial plant that is cooled with the water. An average power plant, for example a NUON multifuel power plant in the Netherlands, produces about 571429 kg of CO2 per hour. The amount of CO2 that is transferred to the water to adjust the pH to a level between 6 and 7.5, more preferred to a level between 6.5 and 7.5, is between about 5% and 10% of the total CO2 emission of the plant. The carbon dioxide is optionally treated, for example filtered, prior to

transferring the carbon dioxide to the water to reduce or eliminate toxic substances. The carbon dioxide that is included in the exhaust gas from a plant, for example a power plant, may contain toxic substances such as fine particulate matter and metals, for example lead and arsenic. Methods, for example filtration technologies, that are used to remove these toxic substances are known in the art and include scrubbers, such as wet and dry scrubbers. The invention further provides a cooling system comprising means for transferring carbon dioxide to the cooling water to bring the cooling water at a pH of at most 7.5, wherein the cooling water is not pressurized. Said cooling system is preferably for cooling of an industrial plant, for example a power plant, or other industrial plant such as, for example, a chemical plant including a petroleum refinery and a blast furnace.

Said means for transferring carbon dioxide to the water, preferably cooling water, include means for transferring exhaust gas from a plant, preferably filtered exhaust gas, through the water, for example by an exhaust gas discharging chamber for discharging gas in the form of gas bubbles into said water. Said exhaust gas discharging chamber preferably comprises a porous membrane whereby gas absorption rate is enhanced by a bubble dispersion mechanism. The cooling water may be recycled through a recirculating system or used in a single pass once-through cooling system. In one embodiment, a preferred cooling system according to the invention is a once-through cooling system. The main advantages of a once-through system is that it is a simple type of system and very flexible.

In another embodiment, a preferred cooling system according to the invention is a recirculating system. Recirculating systems may be open if they rely upon cooling towers or cooling ponds to remove heat. If heat removal is accomplished with negligible evaporative loss of cooling water, the recirculating system may be closed. A preferred cooling system, for example for an energy plant is an open recirculating cooling system. Open recirculating cooling systems save a

tremendous amount of fresh water compared to the alternative method, once- through cooling. The quantity of water discharged to waste is greatly reduced in the open recirculating method, and chemical treatment is more economical.

However, cooling by evaporation increases the dissolved solids concentration in the water, raising corrosion and deposition tendencies. In addition, the relatively higher temperatures significantly increase corrosion potential and increase the tendency for biological growth. The transfer of carbon dioxide to the cooling water of an open recirculating cooling system to bring the water at a pH of at most 7.5, preferably at a pH of between 6.5 and 7.5, whereby the water is not pressurized, provides a very economical method of reducing or preventing both scaling and biological growth.

In a preferred cooling system according to the invention, the cooling water is cooled prior to discharging the cooling water back into its source, or prior to its reuse as cooling water. Cooling of the used cooling water is accomplished, for example by a cooling tower. A cooling tower is designed to provide intimate air/water contact. Heat rejection is primarily by evaporation of part of the cooling water. Some sensible heat loss (direct cooling of the water by the air) also occurs, but it is only a minor portion of the total heat rejection. Said cooling tower preferably is a natural or mechanical draft tower and the direction of airflow, relative to the water flow is either counterflow or crossflow. A cooling tower may further aid in reducing the amount of carbon dioxide in the cooling water, prior to discharging the cooling water, for example back into its source.

The invention further provides an industrial plant, for instance a power plant, and/or a chemical plant including a petroleum refinery and a blast furnace, comprising a cooling system according to the invention. Said plant comprises means for transferring carbon dioxide to the cooling water to bring the cooling water at a pH of at most 7.5, preferably at a pH between 6.5 and 7.5, wherein the cooling water is not pressurized.

Figure legends Figure 1

pH in the water columns of the experimental ecosystems. CO2 was applied from day 0 onwards.

Figure 2: Number of juvenile bivalves (Cerastoderma edule) in sediment samples at the end of the study 69 days after the start of the CO2 application.

Figure 3: Biomass (measured as chlorophyll-a fluorescence, by means of a Biotek microtiter plate reader with Gen5 software) of algae settled on substrates at the end of the study 69 days after the start of the CO2 application. Series A and B depict substrates at two different positions in the experimental ecosystem.

Examples

Example 1

Experiments were performed wherein experimental marine ecosystems were exposed to a series of elevated C02-concentrations. The experiments were conducted in outdoor tanks with a total volume of about 5 m³ containing natural seawater and sediment inhabited by a community of planktonic, meio- and macrofaunal organisms. CO2 was continuously added to the water column starting on day 0 in three fluxes so that that pH levels of the water column stabilised around 8.0, 7.5 and 6.8 respectively (Figure 1), corresponding to CO2 pressure of 0.8, 2.6 and 16 m- atm respectively (Table 1). In unexposed control conditions, pH was 8.3 and CO2 pressure 0.4 m-atm.

Table 1 C02 fluxes to the test systems and the related C02 pressure and pH in the water column.

C0₂ flux CO2 pressure pH

(ml/min) (m-atm) (average)

0 0.4 8.3

3 0.8 8.0

15 2.6 7.5

75 16 6.8

Bivalve molluscs and algae are important groups of fouling organisms. Figure 2 depicts the impact of increased CO2 levels on reproduction of mollusks. As representative of bivalve molluscs, the cockle Cerastoderma edule was included in the experimental ecosystems. Although it was clear that shells became less robust at higher CO2 levels, the adults survived all treatments. Reproductive success, however, was strongly affected. At 2.6 m-atm CO2 and higher, reproduction was almost completely inhibited (Figure 2). The poor condition of the adult shells indicates erosion of the shell carbonates. The adults can withstand this situation as long as the shell maintains its protective function. It is likely that under these conditions it is not possible for mollusc larvae to develop the shell that is essential for further development and survival. The impact of the elevated CO2 for fouling prevention concerning the reproductions of bivalve molluscs and the sessile algae is clear at different endpoints.

The impact of increased CO2 levels on sessile algae is depicted in Figure 3.

Roughly speaking algae can appear planktonic, suspended in the water column, or sessile, on sediments and substrates. By definition, only the sessile algae are concerned for fouling. Although CO2 serves as a fertiliser for planktonic algae, our study revealed an opposite effect on sessile algae (Figure 3). The dataset shows a 50% reduction of the algal biomass at 2.6 m-atm CO2 and over 90% reduction at 16 m-atm CO2. The mechanism behind this is not understood yet, but the experimental set-up excludes competition with planktonic algae as the cause.

Conclusion

These results indicate that a CO2 pressure of 1.6 m-atm (resulting in this seawater in a pH of 6.8) is sufficient to prevent the settlement of cockle larvae and to reduce development of sessile algae with 90%. This makes that CO2 has the potential to be used to prevent fouling of marine organisms. Although sensitivity of other species still has to be tested, it is likely that similar results will be found with fresh water species.

Claims

1. A method of reducing and/or preventing fouling on a surface of a

component that is in contact with water, the method comprising: transferring carbon dioxide to the water to bring the water at a pH of at most 7.5, whereby the water is not pressurized.

2. The method according to claim 1, wherein the water is sea water.

3. The method according to claim 2, whereby the amount of carbon dioxide that is transferred to the sea water is at least 10 mg CO2/L.

4. The method according to any one of the previous claims, whereby the water is for cooling of an industrial plant, for example a power plant.

5. The method according to any one of the previous claims, whereby the carbon dioxide is produced by a plant that is cooled with the water.

6. The method according to any one of the previous claims, whereby the water is filtered prior to transferring carbon dioxide to the water.

7. The method according to any one of the previous claims, whereby the carbon dioxide is filtered prior to transferring the carbon dioxide to the water.

8. Cooling system comprising means for transferring carbon dioxide to the cooling water to bring the cooling water at a pH of at most 7.5, whereby the cooling water is not pressurized.

9. Cooling system according to claim 8, for cooling of an industrial plant, for example a power plant.

10. Cooling system according to claim 8 or claim 9, wherein the cooling water is sea water.

11. Cooling system according to any one of claims 8-10, which is a once- through system.

12. Cooling system according to any one of claims 8-10, which is a recirculating system.

13. Cooling system according to any one of claims 8-11, wherein the cooling water is cooled prior to discharging the cooling water.

14. Cooling system according to claim 12, wherein the cooling water is cooled prior to its reuse as cooling water.

15. Industrial plant, comprising a cooling system according to any one of claims 8-14.