MULTI-STAGE EXPANSION EVAPORATOR

Abstract: Each stage of the evaporator has a heat exchanger com­ partment (7,9,10,11) and an evaporation compartment (2,3,4,6) in open communication. Liquid is heated as it passes in one direction through a heat exchanger conduit (28) in the heat exchanger chambers and then evaporated as it passes in counter-flow through the evaporation chambers. To provide a sufficient degree of control of liquid levels in the evaporation compartments, a circulation conduit (32) with a control valve (33) is arranged to convey the heated fluid directly from the discharge chamber (31) to the evaporation compartment of a selected one of the last stages.

Description: "Multi-stage expansion evaporator" The invention relates to a multi-stage expansion evaporator, in particular one of the type having a plurality of stages each comprising a heat exchanger compartment in open connection with an evaporation compartment, with series counterflow circulation, liquid being heated as it flows in one direction through a heat exchanger conduit, the last passing through the heat exchanger compartments and being evaporated as it flows in counterflow through the evaporation compartments. Multi-stage expansion evaporators have been proposed in which both heat exchangers and evaporation compartments are arranged in horizontal series, while others are proposed where the heat exchangers and evaporation compartments are arranged vertically in the direction of circulation. In the case of the latter, vertical type of evaporator, it has been proposed to maintain a fluidised granular bed within the heat exchanger tubes during operation. See Dutch Patent Application 75.05869. Although the invention relates in principle to both of these types of multi-stage expansion evaporators, it will be explained below particularly with reference to the "vertical multi-stage expansion evaporator" type with fluidised bed heat exchanger. An outline diagram of a vertical evaporator with fluidised bed heat exchanger appears in Fig. 1 of the accompanying drawings. This apparatus is arranged like a counterflow heat exchanger. A pure or impure feed is supplied at point 1 at a temperature T1 and is gradually heated up to a temperature T2 on passing in series through the closed conduits of heat exchangers 7,8,9,10 and 11. These heat exchanger compartments are in open connection with evaporation compartments 2,3,4,5 and 6, heat exchanger 7 being connected to compartment 6, heat exchanger 8 to compartment 5, etc. External heat is supplied to the system by means of a heat exchanger 12 in which the feed is increased to a temperature T3 before it travels to a discharge chamber 31. The heated feed then flows from the discharge chamber 31 through the evaporation compartments 2 to 6 consecutively, a part of the feed evaporating in each evaporation compartment and heat being transferred to the rising feed by condensation of moisture in heat exchangers 7 to 11. The condensate forming in the heat exchangers is collected in troughs 13 to 17 which overflow into each other. The non-evaporated feed flows through permanent throttle openings 18, 19, 20 and 21, and possibly partly through variable throttle openings 22,23,24 and 25 from compartment to compartment. Flows of (a) residual feed and of (b) the condensate formed leave the system at points 26 and 27 at temperatures T4 and TS. The feed of such expansion evaporators commonly consists mainly of water. While reference will usually be made below to water or water vapour, the invention should be regarded as being applicable to other fluids and their vapours. In the particular known embodiment described here, the heat exchangers 7 to 12 comprise a number of vertical tubes 28 which are filled with particles 29. When the apparatus is operating, the particles 29 are kept fluidised. Various measures have been proposed to ensure that fluidisation occurs uniformly in all tubes as the feed water circulates from a distributor box 30 to the discharge chamber 31. Particularly when a fluidised bed is used in the heat exchanger tubes 28, only small variations are permissible in the speed at which the feed water flows through the tubes, though even in multi-stage expansion evaporators of a type where no fluidised bed is used, the aim must still be relatively little variation in the speed of flow, in the interests of optimum operation. If the flow speeds in the tubes 28 are too low, the fluidised bed will drop so far down the tubes 28 that part of the heat-transferring surface of these tubes is no longer in contact with the fluidised particles 29, which is detrimental to heat transfer rates. If the feed water flows too fast in the tubes 28 the granulate will be rinsed out of the discharge chamber 31. Various conditions may lead to major fluctuations in the liquid level in the evaporation compartments 2 to 5. For example, this may happen when the apparatus is started up (when there are as yet no differences in vapour pressure as between the compartments) or when the heat supplied to heat exchanger 12 is altered (so that the differences in vapour pressure between the evaporation compartments may change). In order nevertheless to keep the liquid level in each of the evaporation chambers within limits acceptable for operational purposes, various measured solutions have been proposed. In one known solution of the problem, permanent throttle openings 18 to 21 are provided in addition to variable throttle openings 22 to 25 in at least some of the partition walls between the compartments 2 to 6 (see Fig. 1). The closing mechanisms of the variable throttle openings can be coupled for driving to an adjusting mechanism which can be moved from outside the evaporator. With an increasing number of evaporator compartments, these coupled closing mechanisms can lead to the apparatus becoming complicated. In practice, 30 to 40 evaporator compartments linked in series have already been adopted, and this number can be expected to increase yet further in the future. It has also been proposed that consecutive evaporator compartments be connected to each other via exterior syphons. When the fluid rises above a certain level in an evaporation compartment, the compartment then empties into the next compartment via the syphon. However, syphons are expensive in evaporators with many stages, while they give rise to structural difficulties if the height of the evaporator compartments is reduced. The object of the invention is to achieve sufficient control of the fluid level in the evaporation compartments of a multi-stage expansion evaporator, in a simple structure. In essence, the invention consists of a circulation conduit from the discharge chamber, provided with a control valve and connected to one of the last of the evaporation compartments in the circulation sequence. In this way, excessive levels in certain evaporation compartments can be avoided by conveying part of the water through the circulation conduit, so that the remaining quantity of feed water still flowing through these compartments does not produce an excessive level in them. It is then no longer necessary to fit adjustable throttle openings in the partition walls, in addition to the fixed throttle openings, nor to provide syphons between consecutive evaporation compartments. By one of the last of the evaporation compartments, is meant one of the evaporation compartments in the second half of the evaporator (in the direction of flow of the liquid through the evaporation compartments), and preferably this selected compartment is among the last 30% or even 20% of the compartments. USA patent no. 3,329,583 describes a multi-stage evaporator in which a by-pass line can convey a proportion of the feed from the top of the heat exchanger column directly to an intermediate evaporation compartment. The arrangement shown differs from the present invention (a) in that the feed is drawn off prior to application of external heat (i.e. before the discharge chamber of the present invention) (b) in that the evaporation chamber to which the feed is taken by this by-pass line is not one of the last evaporation chambers and (c) in that the purpose of the use of the by-pass line is to achieve more efficient utilization of heat. Although the invention can be applied to multistage expansion evaporators generally, it has been found that the best results can be obtained with the invention by applying it to apparatus in which the heat exchangers and evaporation compartments are each located vertically above each other in series, and in which the heat exchangers comprise tubes filled with fluidisable particles. It is known among experts in this field that the liquid levels in the compartments of a multi-stage expansion evaporator are less sensitive to variation the lower the operating temperature in the compartment, i.e. in a vertical evaporator the lower the evaporation compartment is located in the column. The consequence is that the circulation conduit of the invention need not necessarily be linked to the lowest evaporation compartment. If the liquid levels of compartments located lower permit, the circulation conduit can be connected to a compartment located above the lowermost. In a given situation, the liquid levels can then be distributed to best effect by means of the control valve in the circulation conduit. If satisfactory controllability cannot be achieved in this way, it is also possible for several circulation conduits to be connected to various evaporation compartments through separate control valves. This will generally produce more favourable energy consumption in the installation. A similar effect can also be obtained if several circulation conduits are connected by a common main conduit to the water discharge chamber. It should be noted that these circulation conduits do not restrict the structural height of the evaporation compartments. The proposed apparatus with circulation conduit and control valve can be built up from standard elements, which produces a structurally simpler and, above all, cheaper approach, even if the number of evaporation compartments is very high. It will be clear that control of the liquid levels in the evaporation compartments with the aid of control valves lends itself very readily to automation. Automation can then be achieved, in the manner which will be clear to the expert, based on measurement of the levels in the most critical of the evaporation compartments. When feed water is supplied through the circulation conduit, the compartment or compartments which are connected to this conduit will produce a larger quantity of vapour than the adjoining compartments, which are not connected to the circulation conduit. This give rise to a high vapour pressure in the compartment to which the circulation conduit is connected and therefore to a smaller difference in vapour pressure between this compartment and the preceding one in the direction of flow, so that the flow of liquid in the latter preceding compartment can be inhibited. This can then, in turn, produce an excessive liquid level in the said preceding evaporation compartment. This difficulty can be dealt with in practice in the invention by making the heat exchanger of the stage containing the evaporation compartment connected to a circulation conduit with a larger heat-exchanging surface than other heat exchangers in the apparatus. As a rule, this will mean a greater structural height of the heat exchanger and evaporation compartment involved. By this measure, the pressure in this evaporation compartment can be lower. Another possible way of preventing an excessive liquid level in the preceding evaporation compartment consists in fitting a secondary circulation pipe between the evaporation compartment to which a circulation conduit is connected and the preceding evaporation compartment in the direction of flow of the evaporating liquid. This secondary circulation pipe can be in the form of a syphon. The length needed for this syphon can be reduced by fitting a control valve in the secondary circulation conduit. However, the secondary circulation conduit may not be a syphon, but can be equipped only with a control valve. This secondary circulation pipe can be fitted either at the outside or inside of the apparatus. The preferred embodiment of the invention will now be described by way of example with reference to Figure 2 of the accompanying drawings which is a diagrammatic representation of the multi-stage expansion evaporator of the invention. In Figure 2, the same reference numerals are used as in Figure 1, to denote corresponding parts, and these parts will not be described again. In principle FIg. 2 shows the same apparatus as Fig. 1, corresponding reference numbers relating to corresponding structural elements. However, the variable throttle openings 22 to 25 are omitted from the structure of Fig. 2. Instead, a circulation pipe 32 is fitted between the discharge chamber 31 and evaporation compartment 4, and contains a control valve 33. Compartment 4 is, as illustrated, the penultimate compartment in the sequence, but in practice there will usually be many more stages and the compartment selected for connection of the circulation conduit may be another one. The height H of the heat exchanger 9 and the evaporation compartment 4 is greater than the height h of the adjoining heat exchanger and evaporation compartment 10 and 3 which have a height h. This prevents the liquid level in evaporation compartment 3 from rising too high, as discussed above. Instead of using this difference in height, the level in evaporation compartment 3 can also be controlled by means of a secondary circulation pipe 34 between compartments 3 and 4. This secondary circulation pipe can take the form of a syphon (as drawn), and a control valve 35 can also be fitted to it. It should be noted that it is, of course, possible for the circulation pipe 34 not to be in syphon form and to have only a control valve 35 fitted in it, while these measures may, further, be combined separately or jointly with a difference in height between compartments 3 and 4. It should further be noted that the most advantageous operation can be achieved if the circulation pipes 32 and 34 are closed off during normal stable operation. Then, a correction may be applied only on a change in the stable operation, by causing liquid to flow through the pipe 32 and, possibly also through the pipe 34.

Claims: CLAIMS: 1. Multi-stage expansion evaporator having a plurality of stages each comprising an evaporation chamber (2,3,4,6) and a heat exchanger chamber (7,9,10,11) in open communication with each other and a heat exchanger conduit (28) extending through the heat exchanger chambers to form a path for flow of liquid being heated in one direction through the sequence of stages, the evaporation compartments being connected together to form a path for flow of liquid being evaporated in the opposite direction through the sequence of stages, there being a discharge chamber (31) for the heated liquid from the heat exchanger conduit and means for controlling the liquid level in the evaporation compartment, characterised in that: said means for controlling liquid level comprise at least one circulation conduit (32) connecting the discharge chamber (31) to a selected one of the last evaporation compartments in the sequence, and a control valve (33) in said circulation conduit (32). 2. An evaporator according to claim 1 having at least ten stages wherein said selected stage is one of the four stages adjacent said first stage. 3. An evaporator according to claim 1 or claim 2 wherein the stages are located one above another and said heat exchange conduit comprises,in each stage, a plurality of pipes containing particles fluidisable in the flow of liquid. 4. An evaporator according to any one of claims 1 to 3 having a plurality of said circulation conduits, each with a said control valve, connected respectively to a plurality of said selected stages. 5. An evaporator according to claim 4 wherein said plurality of circulation conduits are connected into said discharge chamber as a common conduit which is subsequently branched. 6. An evaporator according to any one of claims 1 to 5 wherein the heat exchanger surface of the said selected stage to which the circulation conduit is connected has a larger effective area than the heat exchanger surface of stages to which a said circulation conduit is not connected. 7. An evaporator according to any one of claims 1 to 6 wherein a secondary circulation conduit (34) connects the evaporation compartment of said selected stage to the evaporation compartment of the next preceding stage in the sequence in the direction from final stage to first stage. 8. An evaporator according to claim 7 wherein said secondary circulation conduit is in the form of a syphon. 9. An evaporator according to one of claims 7 and 8 wherein said secondary circulation conduit has a control valve for control of fluid flow therethrough.

Inventors: KLAREN, DICK, GERRIT, DR. IR.
Applicants: ESMIL B.V.
Application year: 1981
Main classification: B01D3
IPC codes: C02F1, B01D1, B01D3