ROTARY HEAT AND/OR MASS TRANSFER ARRANGEMENTS

Abstract: A rotary heat and/or mass transfer arrangement in which a liquid component undergoes heat and/or mass transfer with a vapour component comprises a rotor (10) on which a layer of fluid is applied by nozzles (16). The flow across the rotor is actively disturbed by means of a radial row of nozzles (20), to enhance the heat and/or mass transfer coefficients.

Description: Rotary Heat and/or Mass Transfer Arrangements This invention relates to rotary heat and/or mass transfer arrangements . In particular, though not exclusively, the invention is concerned with heat/mass transfer enhancements in apparatus which makes use of process intensification, for example in a rotary absorption heat pumps . Examples of such pumps are disclosed in U.S. Patent No. 5,009,085 and our co-pending International Patent Application No. PCT/GB96/02486 , the entire contents of which are incorporated herein by reference. In such apparatus it is common to make use of rotating surfaces to provide thin films for the transference of heat and mass. For example, in one region of a typical rotary absorption heat pump, a stream of a working mixture which is rich in a volatile component is directed onto a radially inner surface of a rotating generator wall through a single outlet pipe, the other side of the wall receiving heat from a gas burner. To provide an acceptable cycle efficiency it is extremely important to maximise the heat and mass transfer from the generator wall. Earlier work in this field, (for example Cross, W.T. and Ramshaw, C. Process Intensification: Laminar Flow Heat Transfer. Chem. Eng. Res. Des . , Vol. 64, pp 293-301) indicates that, theoretically, heat and mass transfer coefficients in laminar flow situations can be equivalent to or better than their turbulent counterparts and so it would be expected that laminar flow should be maintained. Surprisingly we have found that, by redesign of the system, it is possible to achieve far greater heat and mass transfer rates, by deliberately disturbing the fluid film, e.g. by wave generation or wake interaction. Accordingly, in one aspect of this invention, there is provided a rotary heat and/or mass transfer arrangement, comprising : a rotor means for being rotated in use; means for delivering a supply of liquid to a radially inner region of a surface of said rotor to provide a fluid film which flows over said surface accompanied by heat and/or mass transfer to or from said liquid, and means for disturbing said flow, thereby to enhance at least one of said heat and mass transfer. We have found that by disturbing the flow, the heat and mass transfer coefficients may be increased. Generally we have found that the disturbance creates waves or a wake interaction which enhance mass and heat transfer. This arrangement is particularly appropriate where a liquid/vapour interaction occurs at the exposed surface of said liquid, for example the absorption of vapour into the liquid, the giving off vapour from the liquid, or chemical absorption or chemical reactions at the surface thereof. Preferably, said delivering means comprises a plurality of nozzle means disposed around the rotary axis of said rotor, to provide in use a film thickness m which the non- uniformities are reduced compared to those generated by use of a single delivery nozzle means. We believe that the combination of a substantially uniform film thickness applied by the plurality of nozzle means, and suitable disturbance of the flow either by a main nozzle means, or by a recirculating nozzle means, can increase the heat transfer coefficient by up to 2, and the mass transfer coefficient by up to 2. The plurality of nozzle means may in certain embodiments also constitute the means for disturbing said flow. Thus by suitable location and direction of the liquid jets, a wave generation or wave interaction effect may be set up. For a recirculating arrangement, flow leaving the rotor means may be collected and recirculated to be directed back on to the rotor by means of one or more disturbing nozzle means directed towards the surface of said rotor means. Preferably, a plurality of additional nozzle means are directed at different radial positions thereby to provide a re-stirring of the film and consequently mixing of concentration and temperature profiles within the film for each complete revolution of the rotor. In this way, the local heat and mass transfer rates may be increased. These arrangements may be applied to any of the "rotating disc" processes within a rotary absorption heat pump. Accordingly, in another aspect, this invention extends to a rotary absorption heat pump incorporating one or more rotary heat and/or mass transfer arrangements as described above . We have found that the cycle efficiency of the heat pump can be substantially enhanced by using these arrangements . In another aspect, there is provided a method of enhancing the heat or mass transfer coefficient in a rotary system comprising a rotor over which liquid is required to flow in use accompanied by heat and/or mass transfer to or from said liquid, said method comprising disturbing said flow, thereby to cause at least partial re-stirring and/or re-mixing of liquid within said flow. In another aspect, the invention extends to a rotary heat and/or mass transfer arrangement comprising: a rotor for being rotated in use; means for delivering a supply of liquid to a radially inner region of a surface of said rotor to flow in use over said surface accompanied by heat and/or mass transfer to or from said liquid, wherein said means for delivering comprises a plurality of nozzle means disposed about the rotary axis of said rotor adapted to provide a non-laminar flow of fluid across said rotor. Whilst the invention has been described above it extends to any inventive combination of the features set out above or in the following description. The invention may be performed in various ways, and, by way of example only, an embodiment thereof will now be described in detail, reference being made to the accompanying drawing which is a schematic view of a rotary heat and/or mass transfer arrangement. Referring to the Figures, the arrangement comprises a rotor or disc 10 mounted on a shaft 12 for rotation about the shaft axis. The rotor 10 may typically be a generator wall in a rotary absorption heat pump arrangement of the types described in U.S. Patent No. 5,009,085 or in our copending International Patent Application PCT/GB96/02486. In such arrangements it is important to maximise the heat transfer between the rotor and the thin film of fluid flowing over it, and also the mass transfer of vapour from the liquid film. In the illustrated arrangement, the primary flow of fluid to the surface is supplied to a collar 14 having a plurality of nozzles 16 equi-angularly disposed about the rotary axis of the rotor 12. The nozzles 16 are designed to distribute the flow substantially evenly about the inner radial portion of the rotor so that a film of substantially uniform thickness to be set up, but also to impart by the jet action of the nozzles to the formed liquid film a wave or wake interaction effect to cause mixing and stirring of the film and thus to enhance its heat and mass transfer coefficients. The system also includes an arrangement for directing a recirculating flow of fluid to the surface of the rotor 10 through a linear arrangement 18 of jets 20 applied at differing radial positions. On leaving the radially outer edge of the rotor, at least part of the liquid is collected in a sump ring 22, by a pump 24 and pumped to the jets 20. As well as producing an uniform application of fluid the method also provides a re-stirring of the film and consequent re-mixing of concentration and temperature profiles within the film each complete revolution of the rotor. This type of arrangement is particularly applicable when using high viscosity fluids as found in rotary absorption heat pumps (typically 1 to 30 centipoise) which behave in a highly laminar manner and which are not highly stirred within the film thickness. Without the modifications of the present invention, the laminar jet flow would produce a situation where the concentration and temperatures profiles within the liquid film would dominate the transfer rates . By way of example, the typical rotational speed of the rotor in a typical rotary absorption heat pump would be up to 1000 rpm with liquid flow rates of between 10 and 100 grams per second, over the surface of a rotor of typically 50cm in diameter.

Claims: Claims 1. A rotary heat and/or mass transfer arrangement, comprising: - a rotor means for being rotated in use; means for delivering a supply of liquid to a radially inner region of a surface of said rotor to provide a fluid film which flows over said surface accompanied by heat and/or mass transfer to or from said liquid, and means for disturbing said flow, thereby to enhance at least one of said heat and mass transfer. 2. A rotary heat and/or mass transfer arrangement according to Claim 1, wherein .said delivering means comprises a plurality of delivery nozzle means disposed around the rotary axis of said rotor to provide in use a film of substantially uniform thickness. 3. A rotary heat and/or mass transfer arrangement according to Claim 2, wherein said delivery means comprises a common pipe or conduit for supplying fluid to each of said nozzle means. 4. A rotary heat and/or mass transfer arrangement according to any preceding Claim, wherein said disturbing means comprises at least one disturbing nozzle means disposed radially outwardly of said delivery nozzle means. 5. A rotary heat and/or mass transfer arrangement according to Claim 4, including means for collecting fluid passing from said rotor means and for supplying it to said disturbing nozzle means. 6. A rotary heat and/or mass transfer arrangement according to any of Claims 1 to 3 , wherein said means for disturbing comprise said delivery nozzle means arranged such that in use the impingement of the jets from said nozzle means causes non-laminar wave generation or wave interaction. 7. A rotary heat pump incorporating one or more rotary heat and/or mass transfer arrangements according to any of Claims 1 to 6. 8. A method of enhancing the heat or mass transfer coefficient in a rotary system comprising a rotor over which liquid is required to flow in use accompanied by heat -and/or mass transfer to or from said liquid, said method comprising disturbing said liquid to provide a mixed or stirred flow. 9. A rotary heat and/or mass transfer arrangement comprising : - a rotor for being rotated in use; means for delivering a supply of liquid to a radially inner region of a surface of said rotor to flow in use over said surface accompanied by heat and/or mass transfer to our from said liquid, wherein said means for delivering comprises a plurality of nozzle means disposed about the rotary axis of said rotor, adapted to provide a mixed or stirred flow of liquid across said rotor. 10. A two phase, liquid/vapour system in which in use a liquid component undergoes mass and heat transfer with a vapour component, said system comprising:- a rotor means for being rotated in use; means for delivering a supply of liquid to a radially inner region of a surface of said rotor to provide a fluid film which flows over said surface accompanied by heat and/or mass transfer to or from said liquid, and means for disturbing said flow, thereby to enhance at least one of said heat and mass transfer.

Inventors: LORTON ROBERT, WINNINGTON TERENCE LESLIE, LORTON, ROBERT, WINNINGTON, TERENCE, LESLIE
Applicants: INTEROTEX LIMITED, LORTON ROBERT, WINNINGTON TERENCE LESLIE, LORTON, ROBERT, WINNINGTON, TERENCE, LESLIE
Application year: 1998
Main classification: B01D1
IPC codes: B01D1, F25B33, F25B37, F28D11, F28F13