Superheated water

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Superheated water is liquid water under pressure at temperatures between the usual boiling point (100°C) and the critical temperature (374°C). It is also known as subcritical water and pressurised hot water. Superheated water referred to in this article is stable because of an applied over pressure which raised the boiling point, or by heating in a sealed vessel with a headspace, where the liquid water is in equilibrium with vapour at the saturated vapour pressure. This is distinct from the use of the term superheating to refer to water at atmospheric pressure above its normal boiling point, which has not boiled due to a lack of nucleation sites (sometimes experienced by heating liquids in a microwave).

Many of the anomalous properties of water are due to very strong hydrogen bonding. Over the superheated temperature range the extensive hydrogen bonds break down, resulting in properties different from those expected from increased temperature alone. Water effectively becomes less polar and behaves in some respects more like an organic solvent such as methanol or ethanol. Solubility of organic materials and gases increases by several orders of magnitude and the water itself can act as a solvent, reagent and catalyst in a range of industrial and analytical applications, including extraction, chemical reactions and cleaning.

Contents

[edit] Change of properties with temperature

All materials change with temperature, but water shows changes which are much greater than would be expected from temperature considerations alone. Viscosity and surface tension of water drop and diffusivity increases with increasing temperature. [1] Self-ionization of water increases with temperature, and the pKw of water at 250°C is closer to 11 than the more familiar 14 at 25°C. This means that the concentration of hydronium ion (H3O+) is higher, and hence the pH is lower (although the level of hydroxide (OH-) is increased by the same amount so the water is still neutral). Specific heat capacity at constant pressure also increases with temperature, from 4.187 kJ / kg at 25°C to 8.138 kJ / kg at 350°C. The dielectric constant (relative permittivity) decreases significantly as the temperature rises, which has a significant effect on the behaviour of water at high temperatures. [2]

[edit] Explanation of anomalous behaviour

Water is a polar molecule, where the centers of positive and negative charge are separated. In an applied electric field, the molecules are able to align with the field. In water, the extensive hydrogen bonded network tends to oppose this alignment, and the degree to which this occurs is measured by the relative permittivity. In water, polarity shifts are rapidly transmitted through shifts in orientation of the linked hydrogen bonds, and therefore water has a high relative permittivity, about 80 at room temperature. This allows water to dissolve salts, as the attractive electric field between ions is reduced by about 80 fold. [1] As the temperature increases, the thermal motion of the molecules disrupts the hydrogen bonding network, and therefore the relative permittivity decreases with temperature, to about 7 at the critical temperature. At 205°C the relative permittivity has fallen to 33, which is the same as methanol at room temperature. Thus from 100°C to 200°C water is behaving like a water / methanol mixture. The disruption of the extended hydrogen bonding is also responsible for much of the anomalous behaviour of superheated water, as extra energy needs to be supplied to break the bonds (increased heat capacity), and the molecules move more freely (viscosity, diffusion and surface tension effects).

[edit] Solubility in superheated water

[edit] Organic compounds

Organic molecules often show a dramatic increase in solubility in water as the temperature rises, partly because of the polarity changes described above, and also because the solubility of sparingly soluble materials tends to increase with temperature as they have a high enthalpy of solution. Thus materials generally considered “insoluble” can be very soluble in superheated water. The solubility of PAH’s increased by 5 orders of magnitude from 25°C to 225°C[3] and naphthalene, for example, forms a 10% wt solution in water at 270°C, and the solubility of the pesticide chloranthonil with temperature is shown in the table below.[2]

Solubility of Chloranthonil in Water
T (°C) Mole Fraction
50 5.41 x 10-8
100 1.8 x 10-6
150 6.43 x 10-5
200 1.58 x 10-3

Thus superheated water can be used to process many organic compounds with significant environmental benefits compared to the use of conventional organic solvents.

[edit] Salts

Despite the reduction in relative permittivity, many salts remain very soluble in superheated water until the critical point is approached. Sodium chloride, for example, dissolves at 37 wt% at 300°C [4] As the critical point is approached, the solubility drops markedly to a few ppm, and salts are hardly soluble in supercritical water. Some salts do show a reduction in solubility with temperature, but this behaviour is less common.

[edit] Gases

The solubility of gases in water is usually thought to decrease with temperature, but this only occurs to a certain temperature, then solubility increases again. For nitrogen, this minimum is 74°C and for oxygen it is 94°C [5] Therefore gases are quite soluble in superheated water at elevated pressures. Above the critical temperature, water is completely miscible with all gasses. The increasing solubility of oxygen in particular allows superheated water to be used for the wet oxidation processes

[edit] Corrosion

Superheated water can be more corrosive than water at ordinary temperatures, and at temperatures above 300°C special corrosion resistant alloys may be required, depending on the other components dissolved in the water. However, continuous use of carbon steel pipes for 20 years at 282°C has been reported without significant corrosion,[6] and stainless steel cells showed only slight deterioration after 40-50 uses at temperatures up to 350°C. [7] The degree of corrosion which can be tolerated depends on the use, and even corrosion resistant alloys can fail eventually. Corrosion of an Inconel U-tube in a heat exchanger was blamed for an accident at a nuclear power station[8]. Therefore, for occasional or experimental use, ordinary grades of stainless steel are probably adequate with continuous monitoring, but for critical applications and difficult to service parts, extra care needs to be taken in materials selection.

[edit] Effect of Pressure

At temperatures below 300°C water is fairly incompressible, which means that pressure has little effect on the physical properties of water, provided it is sufficient to maintain liquid state. This pressure is given by the saturated vapour pressure, and can be looked up in steam tables, or calculated here. [9] As a guide, the saturated vapour pressure at 121°C is 100 kPa, 150°C is 470 kPa, and 200 is 1 550 kPa. The critical point is 21.7 MPa at a temperature of 374°C, above which water is supercritical rather than superheated. Above about 300°C, water starts to behave as a near-critical liquid, and the physical properties, such as density, start to change more significantly with pressure. However, it has been reported that higher pressures increase the rate of extractions using superheated water below 300°C, but this could be due to the effect on the substrate, particularly plant materials, rather than affecting the water properties.

[edit] Energy Requirements

The energy required to heat water is significantly lower than that needed to vaporize it, for example for steam distillation[10] and the energy is easier to recycle using heat exchangers. The energy requirements can be calculated from steam tables. For example, to heat water from 25°C to steam at 250°C at 1 atm requires 2869 kJ / kg. To heat water at 25°C to liquid water at 250°C at 5 MPa requires only 976 kJ / kg. It is also possible to recover much of the heat (say 75%) from superheated water, and therefore the energy use for superheated water extraction is less than one sixth needed for steam distillation. This also means that the energy contained in the superheated water is insufficient to vaporise the water on decompression. In the above example, only 30% of the water would be converted to vapour on decompression from 5 MPa to atmospheric pressure.[2]

[edit] Extraction with superheated water

Extraction using superheated water tends to be fast because diffusion rates increase with temperature. Organic materials tend to increase in solubility with temperature, but not all at the same rate. For example, in extraction of essential oils from rosemary[11] and coriander,[12] the more valuable oxygenated terpenes were extracted much faster than the hydrocarbons. Therefore, extraction with superheated water can be both selective and rapid, and has been used to fractionate diesel and woodsmoke particulates.[13] Superheated water is being used commercially to extract starch material from marsh mallow root for skincare applications[14] and to remove low levels of metals from a high-temperature resistant polymer.[15][16]

For analytical purposes, superheated water can replace organic solvents in many applications, for example extraction of PAH’s from soils[17] and can also be used on a large scale to remediate contaminated soils, by either extraction alone or extraction linked to supercritical or wet oxidation. [18]

[edit] Reactions in superheated water

Superheated water, along with supercritical water, has been used to oxidise hazardous material in the wet oxidation process. Organic compounds are rapidly oxidised without the production of toxic materials sometimes produced by combustion. However, when the oxygen levels are lower, organic compounds can be quite stable in superheated water. As the concentration of hydronium (H3O+) and hydroxide (OH-) ions are 100 times larger than in water at 25°C, superheated water can act as a stronger acid and a stronger base, and many different types of reaction can be carried out. An example of a selective reactions is oxidation of ethylbenzene to acetophenone, with no evidence of formation of phenylethanoic acid, or of pyrolysis products. [7] and several different types of reaction in which water was behaving as reactant, catalyst and solvent were described by Katritzky et al. [19] Triglycerides can be hydrolysed to free fatty acids and glycerol by superheated water at 275°C, [20] which can be the first stage in a two stage process to make biodiesel. [21] Superheated water can be used to chemically convert organic material into fuel products. This is known by several terms, including direct hydrothermal liquefaction,[22] and hydrous pyrolysis. There are a few commercial scale applications. The thermal depolymerization or thermal conversion process (TCC) uses superheated water at about 250°C to convert turkey waste into a light fuel oil and is said to be able to process 200 tons of low grade waste into fuel oil a day. [23] The initial product from the hydrolysis reaction is de-watered and further processes by dry cracking at 500°C. The “SlurryCarb” process operated by EnerTech uses similar technology to decarboxylate wet solid biowaste, which can then be physically dewatered and used as a solid fuel called E-Fuel. The plant at Rialto is said to be able to process 683 tons of waste per day. [24] The HTU or Hydro Thermal Upgrading process appears similar to the first stage of the TCC process. A demonstration plant is due to start up in The Netherlands said to be capable of processing 64 tons of biomass (dry basis) per day into oil. [25]

[edit] Chromatography

Reverse phased HPLC often uses methanol / water mixtures as the mobile phase. Since the polarity of water spans the same range from 25 to 205°C, then a temperature gradient can be used to effect similar separations, for example of phenols. [26] The use of water allows the use of the flame ionisation detector (FID), which gives mass sensitive output for nearly all organic compounds. [27] The maximum temperature is limited to that at which the stationary phase is stable. C18 bonded phases which are common in HPLC seem to be stable at temperatures up to 200°C, far above that of pure silica, and polymeric styrene / divinylbenzene phases offer similar temperature stability. [28] Water is also compatible with use of UV detector down to a wavelength of 190 nm.

[edit] See also

[edit] External links

[edit] References

  1. ^ a b Chaplin, Martin (2008-01-04). Explanation of the physical anomalies of water. London South Bank University. Retrieved on 2008-01-15.
  2. ^ a b c Clifford, A.A. (2008-01-04). Changes of water properties with temperature. Retrieved on 2008-01-15.
  3. ^ Miller, D.J. (1998). "Solubility of polycyclic aromatic hydrocarbons in subcritical water from 298 K to 498 K". Journal of Chemical Engineering Data 43 (6): 1043–1047. American Chemical Society. doi:10.1021/je980094g. 
  4. ^ Letcher, Trevor M. (2007). Thermodynamics, solubility and environmental issues. Elsevier, page 60. ISBN 0444527079. 
  5. ^ Guideline on the Henry’s constant and vapor-liquid distribution constant for gases in H2O and D2O at high temperatures. International Association for the Properties of Water and Steam (September 2004). Retrieved on 2008-01-14.
  6. ^ Burnham, Robert N.; Et Al (2001). Measurement of the flow of superheated water in blowdown pipes at MP2 using an ultrasonic clamp-on method. Panametrix. Retrieved on 2008-01-14.
  7. ^ a b Holliday, Russel L.; Yong, B.Y.M., Kolis, J.W., (1998). "Organic synthesis in subcritical water. Oxidation of alkyl aromatics". Journal of Supercritical Fluids 12: 255–260. Elsevier. doi:10.1016/S0896-8446(98)00084-9. 
  8. ^ "Corrosion seen as A-plant accident cause", New York Times, 2000-03-03. Retrieved on 2008-01-15. 
  9. ^ Clifford, A.A. (2007-12-04). Superheated water: more details. Retrieved on 2008-01-12.
  10. ^ King, Jerry W.. Poster 12. Pressurized water extraction: resources and techniques for optimizing analytical applications, Image 13. Los Alamos National Laboratories. Retrieved on 2008-01-12.
  11. ^ Basile, A.; Et Al (1998). "Extraction of Rosemary by Superheated Water". J. Agric. Food Chem. 46 (12): 5205–5209. American Chemical Society. doi:10.1021/jf980437e. 
  12. ^ Eikani, M.H.; Golmohammad, F. and Rowshanzamir, S.. "Subcritical water extraction of essential oils from coriander seeds (Corianrum sativum L.)". 
  13. ^ Kubatova, Alena; Mayia Fernandez and Steven Hawthorne (2002-04-09). "A new approach to characterizing organic aerosol (wood smoke and diesel exhaust particulate) using subcritical water fractionation". PM2.5 and electric power generation: recent findings and implications, Pittsburgh, PA: National Energy Technology Laboratory. Retrieved on 2008-01-10. 
  14. ^ LINK Competitive Industrial Materials from Non-Food Crops Applications: water and superheated water. Newsletter No.8. BBSRC (Spring 2007). Retrieved on 2008-01-08.
  15. ^ Clifford, A.A. (2007-12-04). Applications: water and superheated water. Retrieved on 2008-01-08.
  16. ^ Clifford, Tony (Nov. 5-8, 2006). "Separations using superheated water". 8th International Symposium on Supercritical Fluids. Retrieved on 2008-01-16. 
  17. ^ Kipp, Sabine; Et Al (July 1998). "Coupling superheated water extraction with enzyme immunoassay for an efficient and fast PAH screening in soil". Talanta 46 (3): 385–393. Elsevier Science BV. doi:10.1016/S0039-9140(97)00404-9. 
  18. ^ Hartonen, K; Kronholm and Reikkola (2005). Sustainable use of renewable natural resources – principles and practice. Chapter 5.2 Utilisation of high temperature water in the purification of water and soil: University of Helsinki Department of Forest Ecology. ISBN 952-10-2817-3. 
  19. ^ Katritzki, A.R.; S. M. Allin, M. Siskin (1996). "Aquathermolysis: reaction of organic compounds with superheated water". Accounts of Chemical Research 29: 399–406. American Chemical Society. doi:10.1021/ar950144w. 
  20. ^ King, Jerry W.; Holliday, R.L. and List, G.R. (December 1999). "Hydrolysis of soubean oil in a subcritical water flow reactor". Green Chemistry: 261–264. Royal Society of Chemistry. 
  21. ^ Saka, Shiro; Kusdiana, Dadan. NEDO “High efficiency bioenergy conversion project”R & D for biodiesel fuel (BDF) by two step supercritical methanol method. Retrieved on 2008-01-12.
  22. ^ Biomass Program, direct Hydrothermal Liquefaction. US Department of Energy. Energy Efficiency and Renewable Energy (2005-10-13). Retrieved on 2008-01-12.
  23. ^ About TCP Technology. Renewable Environmental Solutions LLC. Retrieved on 2008-01-12.
  24. ^ Sforza, Teri (2007-03-14). New plan replaces sewage sludge fiasco. Orange county register. Retrieved on 2008-01-27.
  25. ^ Goudriaan, Frans; Naber, Jaap and van den Berg, Ed. Conversion of Biomass Residues to Transportation Fuels with th HTU Process. Retrieved on 2008-01-12.
  26. ^ Yarita, Takashi; Nakajima, R. and Shibukawa, M. (February 2003). "Superheated water chromatography of phenols using poly(styrene-divnylbenzene) packings as a stationary phase". Analytical Sciences 19: 269–272. The Japan Society for Analytical Chemistry. doi:10.2116/analsci.19.269. 
  27. ^ Smith, Roger; Young, E. and Sharp, B.. Superheated water chromatography – flame ionization detection. Retrieved on 2001-01-12.
  28. ^ Smith, R. M.; Burgess, R.J. (1996). "[(http://www.rsc.org/publishing/journals/article.asp?doi=ac9963300327 Superheated water – a clean eluent for reverse phase high performance chromatography]". Analytical Communications 33: 327–329. Royal Society of Chemistry. doi:10.1039/AC9963300327.