NZ736744B2 - Apparatus and method for improved evaporation drying - Google Patents

Abstract

Prior art evaporation drying systems in the art suffer from problems such as lack of efficiencies of the drying process, limits in reduction of the moisture content of the treated sludge, lack of quality of the end products, large foot print of the prior apparatuses, and excessive time required for heating and cooling down. The present invention provides an apparatus 100 for drying a substance 190, the apparatus 100 comprising at least one roller 121 rotatable about a central axis; a first belt 112 having a first side 1 12' and a second side 1 12", the first side 1 12' of the first belt 1 12 adapted to receive the substance 190; and a plurality of heat induction elements 123 arranged to induce heat in the first belt 1 12 to heat the substance 190, where in operation, the first belt 1 12 urges via its first side 1 12', the substance 190 towards a portion of an exterior circumferential surface of the roller 121, and the substance 190 is heated to remove fluids from the substance 190. heating and cooling down. The present invention provides an apparatus 100 for drying a substance 190, the apparatus 100 comprising at least one roller 121 rotatable about a central axis; a first belt 112 having a first side 1 12' and a second side 1 12", the first side 1 12' of the first belt 1 12 adapted to receive the substance 190; and a plurality of heat induction elements 123 arranged to induce heat in the first belt 1 12 to heat the substance 190, where in operation, the first belt 1 12 urges via its first side 1 12', the substance 190 towards a portion of an exterior circumferential surface of the roller 121, and the substance 190 is heated to remove fluids from the substance 190.

Description

(12) Granted patent specificaon (19) NZ (11) 736744 (13) B2 (47) aon date: 2021.12.24 (54) APPARATUS AND METHOD FOR IMPROVED EVAPORATION DRYING (51) Internaonal Patent ficaon(s): C02F 11/12 F26B 3/347 F26B 17/02 F26B 23/00 F16C 13/00 (22) Filing date: (73) Owner(s): 2016.04.06 SINGNERGY CORPORATION PTE LTD (23) Complete specificaon filing date: (74) Contact: 2016.04.06 AJ PARK (30) Internaonal Priority Data: (72) Inventor(s): SG 02704V 2015.04.07 CHUA, Keng Tai (86) Internaonal Applicaon No.: (87) Internaonal aon number: WO/2016/163955 (57) Abstract: Prior art evaporaon drying systems in the art suffer from problems such as lack of efficiencies of the drying process, limits in reducon of the moisture content of the treated sludge, lack of quality of the end products, large foot print of the prior tuses, and excessive me required for heang and cooling down. The present invenon provides an tus 100 for drying a substance 190, the apparatus 100 comprising at least one roller 121 rotatable about a central axis; a first belt 112 having a first side 1 12' and a second side 1 12", the first side 1 12' of the first belt 1 12 adapted to receive the substance 190; and a plurality of heat inducon elements 123 arranged to induce heat in the first belt 1 12 to heat the substance 190, where in operaon, the first belt 1 12 urges via its first side 1 12', the substance 190 towards a poron of an exterior circumferenal surface of the roller 121, and the substance 190 is heated to remove fluids from the substance 190.

NZ 736744 B2 APPARATUS AND METHOD FOR IMPROVED EVAPORATION DRYING FIELD OF THE INVENTION The present invention relates generally to apparatus and methods for the drying of substances, in particular but not limited to evaporation drying of .

BACKGROUND TO THE INVENTION The ing discussion of the background to the invention is ed to facilitate an understanding of the present invention. However, it should be appreciated that the discussion is not an acknowledgment or admission that any of the material referred to was published, known or part of the common general knowledge in any jurisdiction as at the priority date of the application.

Sludge is a semi-solid slurry which includes but is not limited to sewage sludge, biogas es, paper sludge, and food and beverage sludge. Sludge variants can carry heavy metals, toxins, pollutants and pathogens. ore, if sludge is not properly treated before disposal, there will be a risk of disease spread, heavy metal poisoning and environmental damage. Treatment of sewage or wastewater sludge generated from wastewater treatment plants typically comprises the following steps: thickening, dewatering and drying. Drying by heat removes the sludge’s moisture content and can destroy pathogens and neutralise toxins. The removal of moisture and application of heat to dry the sludge can result in safe and easy handling of the dried sludge for ream ent/disposal.

Several methods have been developed to dry sludge and these include but are not limited to convection, radiation and indirect (contact or conduction) drying methods. In convection s, heated dry air is brought into contact with the sludge in a drum or belt dryer; in radiation s, heat ed by heating elements is used to dry the , where such heat can come from solar radiation or ed heating elements; and in indirect methods, the sludge is brought into contact with a surface heated by a heat source for drying.

US Patent No. 5,091,079 discloses an apparatus which uses two ovens to provide induction heating to reduce sludge especially those sludge containing heavy metal and a vacuum evacuation chamber to draw gases and vapours from the sludge being reduced, where the sludge travels through the apparatus along a single conveyor belt.

KR Patent Registration No. 10-1005086 and KR Patent Registration No. 10- 3 disclose a sludge drying apparatus which uses a heated roller or drum to dry sludge. Thermal oil is used as a g medium where it is pumped to the interior of the roller, and ts heat to the roller’s interior circumferential surface. The conducted heat then travels to the exterior circumferential surface of the roller, against which the sludge being dried is ssed via a belt. There are several disadvantages associated with these drying apparatuses. Firstly, heat is conducted from the side of the sludge in contact with the roller to the other side, where re and evaporated vapour has to travel across the thickness of the sludge in order to escape, since the roller will likely have an impenetrable/nonporous surface to prevent the l oil from leaking out. Therefore thickness of sludge being treated is limited due to the way heat is conducted only at one side of the sludge and the relatively long escape route of the moisture and vapour from one side of the sludge to the other. Secondly, the thermal oil has to be continuously recirculated from the rollers to boilers/heaters to ish any heat loss. During such recirculation, there is inherent heat loss along the thermal oil piping, boiler/heater and portions of the rollers which are not used to dry the sludge, y leading to energy ciencies.

Thirdly, boilers/heaters, l piping and large pumps to circulate the oil will result in a large footprint for the entire apparatus. Fourthly, for single or multiple rollers configurations, the thermal oil is typically drawn from the same source, i.e. a single boiler. Therefore, the drying temperature cannot be accurately controlled and varied at different drying stages. Fifthly, heating temperature is limited by the maximum thermal oil operating temperature. Finally, a substantial amount of time (approximately one hour) is required to warm the apparatuses from room temperature to the desired drying temperature.

Furthermore, as it will be unsafe to conduct maintenance and repair works while the tuses are still hot, a substantial amount of time is required to fully cool the apparatuses down – typically more than 3 hours to cool down and reach 100°C.

Therefore there is a need to alleviate problems in the prior art, such as to increase the encies of the drying process of the prior art apparatuses, further reduce the moisture content of treated sludge, improve the quality of end products, decrease the foot print of the prior apparatuses, and e the time required for heating and cooling down. An additional or alternative need is to at least provide the public with a useful choice.

SUMMARY OF THE INVENTION Throughout this document, unless otherwise indicated to the contrary, the terms “comprising”, “consisting of”, and the like, are to be ued as nonexhaustive , or in other words, as meaning “including, but not limited to”.

The above mentioned need is met at least in part and an improvement in the art is made by an apparatus in accordance with this invention.

In accordance with a first aspect of the invention, there is provided an apparatus for drying a substance, the apparatus comprising: at least one nonmetal roller rotatable about a l axis; a first metal belt having a first and a second side, the first side of the first belt adapted to receive the substance; and one or more heat induction ts ed proximate to and about a portion of a surface of the roller, where in operation, the one or more heat induction elements induce heat in the first belt to heat the substance to remove fluids from the substance, and do not induce heat in the roller, and n the first belt urges via its first side, the nce towards a portion of an exterior circumferential e of the roller.

The fact that the induction heating elements are arranged to heat the first belt allows for a portion of the substance in contact with the first side of the first belt is heated faster than the other portions of the substance, hence creating a shorter moisture and vapour escape route because re and vapour located at the same side as the first belt will evaporate first, and by capillary pressure, draw more moisture and water to that surface. Further, there is increased pressure imparted onto the sludge as the belt compresses the sludge against a portion of the outer circumferential surface of the roller. This increases the compactness and surface area of the sludge that is in contact with the heated belt. As a result, moisture and water evaporate at a much higher rate than the apparatuses in the prior art. Moreover, r sludge can be processed, thereby increasing treatment capacity. Furthermore, instead of using a thermal fluid, the present invention uses induction heating elements which are preferred because firstly, a boiler/heater, piping and pump are no longer required, resulting in the apparatus having better energy efficiency (e.g. less unnecessary heat loss to other components of the tus) and taking up less space; secondly, higher operating atures can be used and more control with accurate and responsive temperature settings at various drying stages can be achieved; and thirdly the desired operating temperature can be achieved in a short period of time and the apparatus can be cooled down quickly.

Preferably, the at least one roller is constructed substantially from a non- metal material. More preferably, the first belt ses a metal, and even more preferably, the first belt is made of fine metal , and n the first belt is porous.

Preferably, at least one heat induction element is arranged within the roller, proximate to and about a portion of an interior circumferential surface of the . ably, at least one heat induction element is arranged proximate to and about the portion of the exterior circumferential surface of the roller, where in ion, the substance and the first belt is driven between the portion of the exterior circumferential surface of the roller and the heat induction element.

Preferably, the apparatus further comprises at least one tensioning means adapted to tension the first belt.

Preferably, the apparatus further comprises a dislodging means for dislodging the substance from the first belt.

Preferably, the apparatus further comprises a second belt having a first and second side, where in operation, the substance is sandwiched between the first side of the first belt and the first side of the second belt, and n the first belt urges via its first side, the substance and the second belt s the n of the exterior circumferential surface of the roller.

Preferably, the second belt comprises a metal, more preferably, the second belt is made of fine metal fibres, and wherein the second belt is porous.

Preferably, the ity of heat induction elements is arranged to induce heat in the second belt to heat the substance.

Preferably, the apparatus has a plurality of rollers, where in ion, the second belt urges via its first side, the substance and the first belt towards a portion of an exterior circumferential e of at least one roller.

Preferably, the apparatus r comprises at least one tensioning means adapted to tension the second belt.

Preferably, the apparatus further comprises a dislodging means for dislodging the substance from the second belt.

Preferably, the apparatus further comprises an exhaust d to remove fluids from the apparatus. ably, the apparatus further comprises a ventilator adapted to remove fluids from a surface of the substance. ably, the apparatus further comprises a device adapted to distribute the substance on the first side of the first belt.

In accordance with a second aspect of the present invention, there is provided a drying apparatus non-metal roller when used in an apparatus according to the first aspect of the present invention, the roller comprising a plurality of projections and a plurality of channels, the projections and channels arranged on a portion of the exterior circumferential surface of the , wherein the channels are d to allow the escape of fluids from the substance during operation.

Preferably, the projections are constructed from a material different from the material of the roller.

Preferably, the plurality of projections comprise ridges arranged substantially along the length of the roller on the exterior circumferential surface of the roller. ably, the plurality of projections comprise ridges arranged circumferentially on and around a portion of the exterior circumferential surface of the roller.

Preferably, the exterior circumferential surface of the roller comprises channels to permit the escape of .

Preferably, the plurality of projections and channels are arranged on a surface of a , and wherein the roller is adapted to fit into the sleeve.

Preferably, the roller comprises a metal layer on a n of the exterior circumferential surface of the roller.

In accordance with a third aspect of the present invention, there is provided a method of drying a substance, the method comprising the steps of: distributing the substance on a first metal belt having a first and a second side, the first side of the first belt d to receive the substance; inducing heat in the first belt via one or more heat induction elements arranged proximate to and about a portion of a surface of at least one non-metal roller rotatable about a central axis, to heat the substance to remove fluids from the substance, wherein heat is not induced in the roller by the one or more heat induction elements; and urging the substance via the first side of the first belt towards a portion of an exterior circumferential surface of the roller.

Preferably, at least one heat induction element is arranged within the roller, proximate to and about a portion of an interior ferential surface of the roller. ably, at least one heat induction element is arranged proximate to and about the portion of the or ferential surface of the roller, and wherein the method further comprises the step of driving the substance and the first belt between the portion of the or circumferential surface of the roller and the at least one heat induction elements.

Preferably, the method further comprises tensioning the first belt.

Preferably, the method r comprises the step of ging the substance from the first belt.

Preferably, the method further comprises the step of sandwiching the substance between a first side of a second belt and the first side of the first belt, and urging via the first side of the first belt, the substance and the second belt towards a portion of the exterior circumferential e of the roller.

Preferably, the method further comprises the step of inducing heat in the second belt via the heat induction elements to heat the substance.

Preferably, the method r comprises the step of urging via the first side of the second belt, the substance and the first belt towards a portion of an exterior ferential surface of at least one roller, wherein there is a plurality of rollers.

Preferably, the method r comprises tensioning the second belt.

Preferably, the method further comprises the step of dislodging the substance from the second belt.

Preferably, the method further comprises the step of removing fluids via an exhaust.

Preferably, the method further comprises the step of removing fluids from a surface of the substance via a ventilator.

Reference may be made in the description to subject matter which is not in the scope of the ed . That subject matter should be readily identifiable by a person skilled in the art and may assist putting into practice the invention as defined in the appended claims.

BRIEF DESCRIPTION OF THE DRAWINGS The invention will now be described, by way of example only, with reference to the anying drawings, in which: Figure 1 shows an illustrative view of a first embodiment of an tus of the present invention.

Figure 2 shows an enlarged cross-sectional view of an embodiment of a roller of the apparatus of Figure 1.

Figures 2a and 2b show embodiments of a roller of the apparatus of Figure Figure 3 shows an enlarged cross-sectional view of another embodiment of a roller of the apparatus of Figure 1.

Figure 4 shows an illustrative view of a second embodiment of an apparatus of the present invention.

Figure 5 shows an enlarged sectional view of an embodiment of a roller of the apparatus of Figure 4.

Figures 5a and 5b show other embodiments of a roller of the tus of Figure 4.Figure 6 shows an illustrative view of a third embodiment of an apparatus of the present invention.

Figure 7 shows an illustrative view of a fourth ment of an apparatus of the present invention.

Other arrangements of the invention are possible and, uently, the accompanying drawings are not to be understood as superseding the generality of the preceding ption of the invention.

PREFERRED EMBODIMENTS OF THE INVENTION Particular embodiments of the present invention will now be described with reference to the accompany drawings. The terminology used herein is for the purpose of bing particular embodiments only and is not ed to limit the scope of the present invention. Other definitions for selected terms used herein may be found within the detailed description of the invention and apply throughout. Additionally, unless defined otherwise, all technical and scientific terms used herein have the same meanings as ly understood by one or ordinary skill in the art to which this invention belongs. Where le, the same reference numerals are used throughout the figures for clarity and consistency.

The term ance” used throughout the specification refers to a material or materials which contain fluids that needs to be d or reduced, and such materials include but are not limited to industrial waste such as wastewater treatment sludge, food and/or dairy products, food waste and pharmaceutical drugs. “Fluids” used throughout the specification include liquids (e.g. water and moisture) and gases (e.g. vapour).

A “heating element” used throughout the specification may be any suitable element which produces, conducts, convects, radiates and/or induces heat in a component of the apparatus such as the belts, and includes but is not limited to metal, ceramic, composite heating elements. Therefore the term “heat” used throughout the specification includes heating by conduction, tion, radiation and induction. An example of a heating t is a heat induction element (e.g. induction heating coil) or an electric heating coil. ing to Figure 1 which provides a first embodiment of the present invention, a drying apparatus 100 includes a feeder 110, a drying chamber 120, a ventilator 130 and a discharge station 140. The apparatus 100 also es two endless filter belts, upper (second) belt 111 and lower (first) belt 112, processing rollers 121, and heat induction elements 123. As used throughout the specification, a “heat induction element” refers an element which produces an oscillating magnetic field as a result of an ating electrical current passing through it. The oscillating magnetic field is capable of ng a magnetic flux and producing eddy currents in a neighbouring metal, which as a result of the resistance of the neighbouring metal, heat is d in the neighbouring metal.

The belt 111 has a first side 111’ and a second side 111’’ and the belt 112 has a first side 112’ and a second side 112’’. The belts 111, 112 are capable of being tensioned by air cylinders 113 which are connected to both shaft ends of take-up rollers 114.

The belts 111 and 112 are made of metal, which includes but is not limited to aluminium, copper, brass, iron, steel, alloys and composites thereof. It would be appreciated that the material selected to form belts 111 and 112 comprises a resistive material which allows for efficient generation of heat by induction and a conductive material which allows for the substantially nous distribution of the heat. The belts 111 and 112 preferably have pores and/or slots. Preferably, the belts 111 and 112 are made of fine metal wire, where the belts 111, 112 are porous with very fine pore size. The belts 111, 112 are ably porous so that the magnetic fields and induced currents generated by the heat induction elements 123 can effectively penetrate the belts 111, 112 and efficiently heat the belts 111, 112. However depending on ation, it would be appreciated that the belts 111, 112 may be made from other suitable material, such as synthetic fabrics, which can incorporate metals that can be heated via induction by heat induction elements 123.

The processing rollers 121 are preferably constructed substantially from a non-metal material, which es but is not limited to ceramics, glass , and composites thereof. Preferably, at least the cylindrical portion of the rollers 121, to which the belts 111, 112 will be in t with during operation of the present ion, are made from a non-metal al. Even more preferably, the processing rollers 121 do not se metal at all. The absence of metal or minimal amount of metal in the processing s 121 will ensure that heat does not unnecessarily get induced in the rollers 121 by the heat induction elements 123. This will allow for more effective energy transfer and energy utilization of the apparatus 100 since the heat ion ts 123 will only induce heat in the belts 111, 112 for heating the sludge 190. Each processing roller 121 is rotatable about their own central axis in, for example, a direction A. Depending on the placement of the processing roller 121, said roller may rotate in a clockwise or anticlockwise direction when viewed from one side of the apparatus 100 – for example, processing roller 121a is rotating in an anticlockwise direction as viewed in Figure 1. When in operation, a motor (not shown) rotates the processing rollers 121 which in turn move and drive the belts 111, 112 along with input sludge 190 through the drying chamber 120. It would be understood that the belts 111, 112 may be driven by another roller which is not a processing roller 121, or by any other suitable means. It would also be understood that only one g means may be involved in moving and driving belts 111, 112.

Figure 2 provides an ed cross-sectional view of an embodiment of the roller 121, the belts 111, 112 and sludge 190 of Figure 1. Heat induction elements 123 are arranged within the roller 121, proximate to and about a portion of an interior circumferential surface of the roller 121. The number of heat ion elements 123 installed within roller 121 will depend on application and requirements. It is advantageous for the heat induction elements 123 to be d within the roller 121, to provide modularity to the rollers 121 which allows for easier setting up of the apparatus 100 since each roller 121 may be supplied and installed in apparatus 100 as a single module. As a result of the modularity of the rollers 121, the entire apparatus 100 will require less space to operate. The modular capability of the roller 121 also improves customization of the roller 121 where each roller 121 in the apparatus 100 may have different es, e.g. dimensions, number of heating elements 123 and characteristics of exterior circumferential surfaces. Heat induction elements 123 are preferably stationary during operation of the apparatus 100 so that optimal heat induction is achieved at the portion where the belts 111, 112 are in maximum contact with the roller 121. However depending on application, the heat induction elements 123 may rotate together with the roller 121 when in operation, about the l axis of roller 121. The roller 121 also includes a hollow shaft 150, about which the roller 121 rotates in operation and to which the roller 121 is attached to the apparatus 100, and an inlet 151 for cables for powering heat induction cables 123. It will be appreciated that the distance between the heat induction elements 123 and the or circumferential surface of the rollers 121 may be individually adjustable depending on ation and requirements.

The heat induction ts 123 are connected to a source of high frequency electrical power source which is capable of providing high frequency alternative current (not shown). Magnetic fields and induced currents are produced at the heat ion elements 123. Examples of suitable heat induction ts used in the generation of heat in the belts 111, 112 are described in US Patent No. 402 and US Publication No. 2012/0318461 A1. It will be understood that depending on application and requirements, other forms of ion heating methods and induction heating elements may be used. It would be appreciated that other forms of heating elements, e.g. electric heating coils which transmit heat via convection, conduction and/or radiation may also be used in the present invention, as a replacement of or preferably as an addition to heat induction elements 123. The use of heat induction elements 123 allow for the operating ature of drying apparatus 100 to be reached very quickly from room temperature, within a few seconds, and also allows the drying apparatus 100 to be cooled down very quickly, within a few minutes, which can be assisted by cooling means known in the art, e.g. a fan or blower. ing temperatures of drying apparatus 100, can range from 100°C to 400°C, preferably range from 200°C to 400°C, and even more preferably, range from 200°C to 300°C.

Temperatures as high as 400°C, more ably 350°C, are preferred for certain inorganic sludge, while atures as low as or slightly above 100°C are preferred for certain non-sludge drying applications.

The exterior circumferential surface of roller 121 has projections 128 which are integral and unitary with the roller 121. Projections 128 may be formed from the exterior circumferential surface of roller 121. tions 128 may be ed on the entire exterior circumferential surface of the roller 121 or a portion thereof.

The projections 128 preferably have a hemispheric cross-sectional shape as shown in Figure 2. Therefore in operation, the second sides 111’’, 112’’ of the belts 111, 112 will be in contact with the apical portion of the hemispheric projections 128. However depending on application, the projections 128 may have other cross-sectional shapes, e.g. a polygonal cross-section. When belts 111, 112 are heat up, liquid at the outer side of sludge 190 will turn into vapour 195a and escape through the belts 111, 112. Vapour 195a will escape through the outer belt (i.e. the belt furthest from roller 121, which is lower (first) belt 112 in Figure 2) as shown by arrows B’ and vapour 195a will escape through the inner belt (i.e. the belt closest to the roller 121, which is upper (second) belt 111 in Figure 2) through channels 129 as shown by arrows B’’. Projections 128 may be te projections or as shown in Figure 2a, projections 128 are ridges 128 that run substantially along the length of the roller 121 on its exterior circumferential surface. Ridges 128 define channels 129 which also run substantially along the length of the roller 121 on its or circumferential surface. In an alternative ement as shown in Figure 2b, projections 128 comprises ridges 128 arranged circumferentially (i.e. transverse the length of the roller 121) on and around a portion of the or circumferential surface of the roller 121. Channels 129 also run circumferentially on and around the exterior ferential surface of the roller 121. This arrangement is able because during operation, shear stress between the belts 111, 112 and the ridges 128 is reduced compared to the arrangement of the ridges 128 in Figure 2a. This in turn reduces wear-and-tear on the roller 121, ridges 128 and belts 111, 112. Moreover, the arrangement of the ridges 128 in Figure 2b allow for vapour 195a escaping from the inner belt, to easily exit via channels 129, for example, at an area where the belt 111, 112 is not in contact with the roller 121. It will be iated that ridges 128 and channels 129 may be formed on a separate sleeve 160, whereby the roller 121 is adapted to fit into the sleeve 160. This will provide for easier customization of the exterior circumferential surface of the roller 121 so that the apparatus 100 may be adapted for various applications.

Figure 3 provides a cross-sectional view of another embodiment of roller 121, where tions 128 are formed from a material different from that of the roller 121. This is advantageous because this leads to better customization, where the material forming projections 128 may have different properties compared to the material forming the roller 121. For example, the tions 128 may be made from a material which can withstand high temperatures (for e atures ranging from 100°C to 400°C), is resistant to wear-andtear and is anti-abrasive, while the roller 121 may be made from a al which can withstand high temperatures (for example atures ranging from 100°C to 400°C) and is strong enough to withstand ssion. Preferably the material forming the projections 128 is a non-metal. Projections 128 may be formed from materials which include but are not limited to ceramic, silicone polymer and composites thereof, and roller 121 may be formed from materials which include but are not limited to ceramics, glass fibers or compositions thereof. Projections 128 are embedded, integrated into and bonded/attached to the exterior circumferential surface of roller 121 by means known in the art, which include is but not limited to welding. As shown in Figure 3, projections 128 have a generally annular section, where substantially half of the cross-sectional area of projections 128 is embedded in the roller 121 along its exterior circumferential e, and the exposed half of the projections 128 come into contact with belts 111, 112 during operation. Projections 128 may be in the form of ridges 128 as shown in Figures 2a and 2b.

The surfaces of s 121 are preferably continuous, i.e. having no slots and/or pores, so that the heat induction elements 123 in the interior of the rollers 121, will not be exposed to fluids, e.g. vapours emitted by the sludge 190, which could damage the heat induction elements 123.

Returning to the embodiment in Figure 1, when in operation, the feeder 110 feeds and distributes the sludge 190 onto the first side 112’ of lower belt 112, and the first side 111’ of upper belt 111 comes into contact with the sludge 190, which is held in between and is sandwiched by the belts 111, 112 before contacting the first processing roller 121a. When in contact with the first roller 121a, the heat induction elements 123 induce heat in the belts 111, 112 via magnetic fields generated by the heat induction elements 123. Preferably, heat is generated concurrently in both belts 111, 112. However it would be appreciated that heat in the upper belt 111 may be ted faster than heat in the lower belt 112 because the upper belt 111 is nearer to the heat induction elements 123 compared to the lower belt 112. In such a situation, the rate of removal of fluids (e.g. ation of re) at the upper belt may be higher than that in the lower belt 112. While the sludge 190 held in between the belts 111, 112 negotiates about the arc of the or circumferential surface of the processing rollers 121, the sludge 190 is squeezed due to radial movement, sing pressure impact and shear on the sludge 190 resulting in higher compactness and larger contact area with belts 111, 112. Using processing roller 121a as an example, when in operation, lower belt 112 urges via its first side 112’, the sludge 190 and the upper belt 111 towards the or circumferential surface of said processing roller 121a, thereby squeezing and compacting the sludge 190. The urging mechanism of the belts 111, 112 towards the exterior circumferential surface of processing rollers 121 is achieved by the tensioning of the belts 111, 112 by air cylinders 113 and take-up rollers 114. The air cylinders 113 and takeup rollers 114 can maintain or vary the tension in the belts 111, 112, and affect the compacting of the sludge 190.

At the beginning of the drying process, fluids within the sludge 190 are evaporated via heat conduction, having contact with the first sides 111’, 112’ of the heated belts 111, 112. As fluids are heated away at the sludge surface (e.g. evaporation of re), areas of low pressure are created at the sludge surface which will cause fluids to flow from inner portions of sludge 190 to the surface of the sludge 190 in contact with the first sides 111’, 112’ of the belts 111, 112 by capillary pressure.

After the first processing roller 121a, the belts 111, 112 and sludge 190 progress to the second processing roller 121b and heat induction elements 123.

At this stage, heat is again generated by heat ion elements 123 in the belts 111, 112 and fluids within the sludge 190 are heated away, similar to the drying process as described above at first processing roller 121a.

Similar heating and drying processes continue in the following third and fourth processing rollers 121c, 121d. As more fluids within the sludge 190 are heated away, e.g. via ation along the drying process, the sludge 190 becomes thinner, which allows for better heat penetration into the centre of the sludge 190.

The number of processing rollers can be increased or reduced ing on the application and ements. The movement speed of the belts 111, 112 and the temperature generated in the belts 111, 112 by heat induction elements 123 are adjustable, which allow a user to easily configure the apparatus 100 to achieve the desired dryness of the nce (e.g. sludge 190) at the end of the drying process. Drying temperature and drying duration are two main parameters in achieving optimal drying of a substance. For drying of inorganic sludge such as hydroxide / metal sludge, short drying duration with high drying temperatures of about 200°C – 400°C would be preferred, where two to four processing rollers 121 would be sufficient. For drying of certain food substances, longer drying duration with low drying temperatures of about 100°C – 200°C would be preferred, where four or more sing rollers 121 would be sufficient.

Immediately after the drying process, the sludge 190 is hot and fluids such as moisture and water vapour are adhered to the surface of dried sludge cake 191. A re ventilator 130 is installed immediately after the drying process to further improve the dryness of sludge cake 191. The moisture ventilator 130 includes two hoods 131 which are d in close proximity to the belts 111, 112. s 132 are installed at the inlets of hoods 131, which create an air draft across the surface of sludge cake 191, thereby removing fluids adhered to the surface of sludge cake 191 and exhaust them to the hood 134 of the drying apparatus 100 via pipes 133. With the fluids removed from the sludge cake’s 191 surface, the fluids are prevented from being re-absorbed back by the dried sludge cake.

A hood 134 located on top of the drying chamber 120 is connected to a blower (not shown). The vapour and gases produced and accumulated during the drying process are removed through the hood 134 for further treatment.

The dried sludge cake 191 proceeds to the discharge station 140 at the end of drying apparatus 100, where two motorized brushes 141 are installed to brush the dried sludge 191 off the belts 111, 112, and also simultaneously clean the belts 111, 112. The sludge cake 191 would be crushed into small pieces 192 as it is brushed off, especially those in a “pancake” shape, and will finally drop into the discharge chute 142. The small pieces of sludge cake 192 increases the total surface area for further evaporation of residual fluids, which as a result, es the dryness of final sludge cake.

In a second embodiment of the present invention as shown in Figure 4, a drying apparatus 200 includes a drying chamber 220 having sing rollers 221 and heat induction ts 223. In this ment, the heat induction elements 223 are arranged proximate to and about a portion of the exterior circumferential surface of the sing rollers 221. Drying apparatus 200 operates in a similar manner as drying apparatus 100, except that when in operation, belts 211, 212 move or are driven between the heat induction ts 223 and the processing rollers 221. The heat induction elements 223 will induce heat in the belts 211, 212 via magnetic fields generated by the heat induction elements 223. Preferably, heat is generated concurrently in both belts 211, 212.

However it would be appreciated that the heat in the belt closer to the heat induction elements 223 may be induced at a faster rate compared to the heat in the belt further away from the heat induction elements 223. In such a situation, the rate of removal of fluids (e.g. evaporation of moisture) at one belt (i.e. the belt that heats up faster) may be higher than that in the other belt.

Figure 5 provides an enlarged cross-sectional view of the roller 221, the belts 211, 212 and sludge 290 of figure 5. Heat induction elements 223 are arranged proximate to and about a portion of the or circumferential e of the processing roller 221. The distance between heat induction elements 223 and belts 211, 212 can be individually adjusted (D) to obtain desired drying results. Depending on the application and ements, this ce may vary.

This distance may also be predetermined such that once an optimal distance is determined, said ce between the heat induction elements 223 and the belts 211, 212 will not change.

As heat is induced in belts 211, 212, fluids, such as moisture, are driven from the sludge 290. Vapour 295a at the outer side of sludge 290 escapes through the ost belt 212 (it would be appreciated that this will depend on which processing roller 221, the belts 211, 212 are positioned) via the slots/pores in the belt 212 as indicated by arrows C’ and vapour 295a at the inner side of the sludge 290 closest to the sing roller 221 escapes through the innermost belt, e.g. belt 211 via slots/pores of belt 211 and slots or pores 222 of the wall of the sing roller 221 as indicated by arrows C’’.

Figure 5a and 5b show a first and second embodiment of the processing roller 221 of Figure 4. In Figure 5a, the processing roller 221 has a circumferential surface 224 with an array of slots 222. The slots 222 allow the escape of vapour, gases and/or moisture from the portion of the sludge 290 closest to the roller 221.

In Figure 5b, the processing roller 221 has rods 226 which are joined onto outer flanges 227 at predetermined ces to create slots 222 on the circumferential surface of the processing roller 221, which allow the escape of vapour, gases and/or moisture from the portion of the sludge 290 closest to the roller 221. The roller 221 is installable in the apparatus 200 via axle or shaft 225. The roller 221 is rotatable about its central axis which runs lengthwise through axle or shaft 225.

Roller 221 is preferably constructed substantially from a non-metal material, which includes but is not limited to ceramics and composites thereof. Preferably, at least the cylindrical portion of the rollers 221, to which the belts 211, 212 will be in contact with during operation of the apparatus 200, are made from a nonmetal material. Even more preferably, the processing rollers 221 do not comprise metal at all. The absence of metal or l amount of metal in the processing rollers 221 will ensure that heat does not unnecessarily get induced in the rollers 221 by the heat induction elements 223. This will allow for more effective energy transfer and energy utilization of the apparatus 200 since the heat induction elements 223 will only induce heat in the belts 211, 212 for heating the sludge 290.

In a third ment of the t ion as shown in Figure 6, a drying apparatus 300 includes a drying chamber 320 having processing rollers 321 and heat ion elements 323. In this embodiment, the heat induction elements 323 are not arranged at and about the exterior circumference of processing rollers 321, but rather, heat induction elements 323 are arranged along and proximate to the second sides 311’’, 312’’ of belts 311, 312, between neighbouring processing rollers 321. In this arrangement, the sludge 390 undergoes sequential g by both belts 311, 312, and compression by the belts 311, 312 and processing rollers 321. Having at least one induction heating element 323 in this arrangement is preferred because drying can occur on both sides of the sludge 390 which allows for thicker sludge to be processed each time. Hence there is an increase in sludge processing capacity. Heating of the surfaces of the sludge 390 in contact with the first sides 311’, 312’ of the belts 311, 312 occur at the same time because heat is concurrently induced in the belts 311, 312 by the heat induction elements 323 positioned at the sides of belts 311, 312. It would however be appreciated that a set of heat induction elements being ed only at the side of one of the belts, may be ient to rently induce heat in both belts 311, 312. Other than the differences between the drying chamber 320, drying chamber 220 and drying chamber 120 as bed above, drying apparatus 300 operates in a similar manner as that of drying apparatus 100 and drying apparatus 200.

A fourth embodiment of the present invention is provided in Figure 7 where a drying apparatus 400 includes one endless filter belt 412 which is driven around a sing roller 421. The belt 412 is made of metal, which includes but is not limited to aluminium, copper, brass, iron, steel, alloys and ites thereof. It would be appreciated that the material selected to form belt 412 comprises a resistive material which allows for efficient tion of heat by induction and a conductive material which allows for the substantially homogenous distribution of the heat. The belt 412 preferably has pores and/or slots. Preferably, the belt 412 is made of fine metal wire, where the belt 412 is porous with very fine pore size.

The belt 412 is preferably porous so that the magnetic fields and induced currents ted by the heat induction elements 423 can effectively penetrate the belt 412 and efficiently heat the belt 412. However depending on application, it would be appreciated that the belt 412 may be made from other suitable material, such as synthetic fabrics, which can incorporate material such as metal so as to allow the induction of heat via the heat induction elements 423 in the belt 412. The belt 412 has a first side 412’ and a second side 412’’.

The processing roller 421 is preferably constructed substantially from a nonmetal material, which includes but is not limited to ceramics, glass fibers, and composites thereof Preferably, the roller 421 ses a layer of metal (not shown) on its exterior circumferential surface. The layer of metal may be a sleeve in which the roller 421 is adapted to fit. The layer of metal will allow for the induction of heat only at the exterior ferential e of the roller 421, for g the sludge 490 that is in contact with the roller 421. The exterior circumferential surface of roller 421 can se projections (not shown), like the tions 128 in Figures 2, 2a, 2b and 3.

During operation, the belt 412 is tensioned by two air cylinders 413 connected to the shaft ends of a take-up roller 414. The processing roller 421 is rotatable about its own central axis. A motor (not shown) rotates the processing roller 421 which in turn moves and drives the belt 412 along with input sludge 490 h the drying chamber 420. It would be understood that the belt 412 may be driven by another roller which is not processing roller 421, or by any suitable means. It would also be tood that only one driving means may be ed in moving and driving the belt 412. A feeder 410 feeds and distributes sludge 490 on the first side 412’ of the belt 412.

Heat induction elements 423 are positioned at the interior of the processing roller 421, about a portion of an interior circumferential surface, and also at the exterior of the processing roller 421, proximate to and about a portion of an exterior circumferential surface. It would be understood that the portion of the interior and exterior circumferential surfaces where the heat ion elements 423 are arranged, can be a ntial portion, whereby the heat induction elements 423 cover most of the interior and exterior circumferential surfaces. The heat induction elements 423 are connected to a source of high frequency energy (not shown). Magnetic fields and induced currents are produced at the heat induction elements 423. The use of heat induction elements 423 allow for the operating temperature of drying apparatus 400 to be reached very quickly from room temperature, within a few seconds, and also allows the drying apparatus 400 to be cooled down very quickly, within a few minutes, which can be assisted by cooling means known in the art, e.g. a fan or blower. The belt 412 and processing roller 421 are in close proximity to the heat induction elements 423, hence the belt 412 and the layer of metal on the roller 421 are heated through induction by the magnetic fields from the heat induction elements 423. Depending on the application, the number of heat induction elements 423 can vary.

While the sludge 490 which is held in between and sandwiched by the belt 412 and processing roller 421 negotiates about the arc of the circumferential surface of the sing roller 421, belt 412 urges via its first side 412’, the sludge 490 towards the or circumferential surface of processing roller 421 such that the sludge 490 is squeezed due to radial nt, increasing pressure impact and shear on the sludge 490, thereby ing in higher compactness and larger contact area with belt 412 and processing roller 421. The urging mechanism of the belt 412 towards the exterior circumferential surface of processing rollers 421 is achieved by the tensioning of the belt 412 by air cylinders 413 and take-up rollers 414. The air cylinders 413 and p rollers 414 can maintain or vary the tension in the belt 412, and affect the compacting of the sludge 490.

Heat induced in the belt 412 and the layer of metal on the roller 421 is directly transferred to the compacted input sludge 490, and the moisture within the sludge ates.

At the beginning of and during the drying process, the fluids within the sludge 490 in contact with the first side 412’ of the belt 412 and the layer of metal on the exterior circumferential surface of processing roller 421 are removed through heat conduction. As fluids are heated away at the sludge surface (e.g. evaporation of moisture), areas of low pressure are d at the sludge surface which will cause fluids to flow from the inner portions of sludge 490 to the surface of the sludge 490 in contact with the first side 412’ of the belt 412 and layer of metal on processing roller 421 by capillary pressure.

At the end of the drying process, the dried sludge on the sing roller 421 is scrapped off from the processing roller 421 with a drum scrapper 445 and a motorized brush 441 to brush off the sludge 490 on the first side 412’ of the belt 412. The final dried sludge 492 drops into a screw conveyor 446 and is discharged from the side of the drying apparatus 400.

It is to be understood that the above embodiments have been provided only by way of exemplification of this invention, such as those detailed below, and that further modifications and improvements thereto, as would be apparent to s skilled in the relevant art, are deemed to fall within the broad scope and ambit of the present invention described. In particular, the following additions and/or modifications can be made without ing from the scope of the invention: • The moisture ventilator may be omitted depending on the application and requirements, or it may be substituted by another suitable device or apparatus.

• The diameter of the processing rollers and accordingly, the cross- sectional circumference of the processing s may vary depending on the ation and requirements.

• Tensioning of the belts need not be achieved only by air cylinders and p rollers, and may be achieved by other suitable means known in the art.

• The number of air cylinders and take-up rollers in the drying apparatus will depend on the ation and requirements.

• The width of the belts (distance from one end of the belt to its other end, where said distance is perpendicular to the direction in which the belt is driven) may be equal or less than the length of the processing s, i.e. the distance from one end of a processing roller to the other end, along the central axis which the processing roller rotates.

Furthermore, although individual embodiments have been discussed it is to be understood that the invention covers combinations of the ments that have been discussed as well.

The invention described herein may e one or more range of values (e.g. distance and temperature). A range of values will be understood to include all values within the range, including the values defining the range, and values adjacent to the range which lead to the same or substantially the same outcome as the values ately adjacent to that value which defines the boundary to the range.

Claims (38)

Claims

1. An apparatus for drying a substance, the apparatus comprising: at least one non-metal roller rotatable about a central axis; a first metal belt having a first and a second side, the first side of the first 5 belt adapted to receive the substance; and one or more heat induction elements ed proximate to and about a portion of a surface of the roller, where in operation, the one or more heat ion ts induce heat in the first belt to heat the substance to remove fluids from the substance, and do 10 not induce heat in the roller, and wherein the first belt urges via its first side, the substance towards a portion of an exterior circumferential surface of the roller.

2. The apparatus according to claim 1, wherein the first belt is made of fine metal fibres, and wherein the first belt is porous.

3. The apparatus according to any one of the preceding claims, wherein at least one heat induction element is arranged within the roller, proximate to and about a n of an interior circumferential surface of the roller. 20

4. The apparatus according to any one of the preceding claims, wherein at least one heat induction element is arranged proximate to and about the n of the or circumferential surface of the roller, where in operation, the substance and the first belt is driven between the n of the exterior circumferential surface of the roller and the heat induction element.

5. The apparatus according to any one of the preceding claims, the apparatus further comprising at least one tensioning means adapted to tension the first belt. 30

6. The apparatus according to any one of the preceding claims, the apparatus further comprising a ging means for dislodging the substance from the first belt.

7. The tus according to any one of the preceding claims, the apparatus further comprising a second metal belt having a first and second side, where in operation, the nce is sandwiched between the first side of the first 5 belt and the first side of the second belt, and wherein the first belt urges via its first side, the substance and the second belt towards the portion of the exterior circumferential surface of the roller.

8. The apparatus according to claim 7, wherein the second belt is 10 made of fine metal fibres, and n the second belt is porous.

9. The apparatus according to claim 7 or 8, where in ion, the one or more heat induction elements induce heat in the second belt to heat the substance and do not induce heat in the roller.

10. The apparatus according to any one of claims 7 to 9, the apparatus having a plurality of rollers, where in operation, the second belt urges via its first side, the substance and the first belt towards a n of an exterior circumferential surface of at least one roller.

11. The apparatus according to any one of claims 7 to 10, the apparatus further comprising at least one tensioning means adapted to tension the second belt. 25

12. The apparatus according to any one of claims 7 to 11, the apparatus further comprising a dislodging means for dislodging the substance from the second belt.

13. The apparatus according to any one of the preceding , the 30 tus further comprising an exhaust adapted to remove fluids from the apparatus.

14. The apparatus according to any one of the preceding claims, the apparatus further comprising a ventilator adapted to remove fluids from a surface of the substance. 5

15. The apparatus according to any one of the preceding claims, the apparatus further comprising a device adapted to distribute the substance on the first side of the first belt.

16. A drying tus non-metal roller when used in an tus 10 according to any one of claims 1 to 15, the roller comprising a plurality of projections and a plurality of channels, the tions and channels arranged on a portion of the exterior circumferential e of the roller, n the ls are adapted to allow the escape of fluids from the substance during ion. 15

17. The roller of claim 16, wherein the roller is operable at a temperature range of 100°C to 400°C.

18. The roller of claim 16 or 17, wherein the projections are constructed from a material different from the material of the roller.

19. The roller ing to any one of claims 16 to 18, wherein the plurality of projections comprise ridges arranged substantially along the length of the roller on the exterior circumferential surface of the roller. 25

20. The roller according to any one of claims 16 to 18, wherein the plurality of projections comprise ridges arranged circumferentially on and around a portion of the exterior circumferential surface of the roller.

21. The roller according to any one of claims 16 to 20, wherein the 30 projections comprise rods, and the channels comprise slots.

22. The roller according to any one of claims 16 to 20, the roller further comprises a sleeve on the exterior circumferential surface thereof, and the plurality of projections and channels are arranged on an outer surface of the sleeve.

23. The roller according to any one of claims 16 to 22, wherein the roller comprises a metal layer on a portion of the exterior ferential surface of the roller. 10

24. A method of drying a substance, the method comprising the steps buting the substance on a first metal belt having a first and a second side, the first side of the first belt adapted to receive the substance; inducing heat in the first belt via one or more heat induction elements 15 arranged proximate to and about a portion of a surface of at least one non-metal roller ble about a l axis, to heat the substance to remove fluids from the substance, wherein heat is not induced in the roller by the one or more heat induction elements; and urging the substance via the first side of the first belt towards a portion of 20 an exterior circumferential e of the roller.

25. The method according to claim 24, wherein at least one heat induction element is arranged within the roller, proximate to and about a portion of an interior circumferential surface of the roller.

26. The method ing to claim 24 or 25, n at least one heat induction element is arranged proximate to and about the portion of the exterior circumferential surface of the roller, and wherein the method r comprises the step of driving the substance and the first belt between the portion of the 30 exterior circumferential surface of the roller and the at least one heat induction element.

27. The method ing to any one of claims 24 to 26, the method further comprising tensioning the first belt.

28. The method according to any one of claims 24 to 27, the method 5 further comprising the step of dislodging the substance from the first belt.

29. The method according to any one of claims 24 to 28, the method further comprising the step of sandwiching the substance between a first side of a second metal belt and the first side of the first belt, and urging via the first side 10 of the first belt, the substance and the second belt s a n of the exterior circumferential surface of the roller.

30. The method according to claim 29, the method further sing the step of inducing heat in the second belt via the one or more heat induction 15 elements to heat the substance, wherein heat is not induced in the roller by the one or more heat induction elements.

31. The method according to claim 29 or 30, the method further comprising the step of urging via the first side of the second belt, the substance 20 and the first belt s a portion of an exterior circumferential surface of at least one roller, wherein there is a ity of rollers.

32. The method according to any one of claims 29 to 31, the method further comprising tensioning the second belt.

33. The method according to any one of claims 29 to 31, the method further comprising the step of dislodging the substance from the second belt.

34. The method according to any one of claims 24 to 33, the method 30 further comprising the step of removing fluids via an exhaust.

35. The method according to any one of claims 24 to 34, the method further comprising the step of removing fluids from a surface of the substance via a ventilator. 5

36. The tus according to claim 1, substantially as herein described with reference to any embodiment disclosed.

37. The roller according to claim 16, substantially as herein described with reference to any embodiment disclosed.

38. The method according to claim 24, ntially as herein described with reference to any embodiment disclosed. WO 63955 PCT/SGZOI