GB2512763A - A method of and apparatus for treating waste and a waste product - Google Patents
A method of and apparatus for treating waste and a waste product Download PDFInfo
- Publication number
- GB2512763A GB2512763A GB1410696.7A GB201410696A GB2512763A GB 2512763 A GB2512763 A GB 2512763A GB 201410696 A GB201410696 A GB 201410696A GB 2512763 A GB2512763 A GB 2512763A
- Authority
- GB
- United Kingdom
- Prior art keywords
- waste
- drying agent
- food
- comminuted
- processed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 291
- 238000000034 method Methods 0.000 title claims abstract description 66
- 239000000843 powder Substances 0.000 claims abstract description 86
- 239000002274 desiccant Substances 0.000 claims abstract description 53
- 239000010794 food waste Substances 0.000 claims abstract description 50
- 238000002156 mixing Methods 0.000 claims abstract description 44
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 43
- 230000007246 mechanism Effects 0.000 claims abstract description 29
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 13
- 230000007423 decrease Effects 0.000 claims abstract description 7
- 239000004570 mortar (masonry) Substances 0.000 claims abstract description 7
- 238000004140 cleaning Methods 0.000 claims description 51
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 235000013305 food Nutrition 0.000 claims description 32
- 239000008187 granular material Substances 0.000 claims description 21
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 20
- 239000000203 mixture Substances 0.000 claims description 20
- 239000010806 kitchen waste Substances 0.000 claims description 19
- 239000000417 fungicide Substances 0.000 claims description 18
- 239000004816 latex Substances 0.000 claims description 18
- 229920000126 latex Polymers 0.000 claims description 18
- 230000000855 fungicidal effect Effects 0.000 claims description 16
- 238000003756 stirring Methods 0.000 claims description 16
- 239000011398 Portland cement Substances 0.000 claims description 15
- 239000011429 hydraulic mortar Substances 0.000 claims description 15
- 239000002174 Styrene-butadiene Substances 0.000 claims description 13
- 239000000920 calcium hydroxide Substances 0.000 claims description 13
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 13
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 13
- 238000001035 drying Methods 0.000 claims description 13
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 13
- 238000007906 compression Methods 0.000 claims description 12
- 239000002245 particle Substances 0.000 claims description 12
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 11
- 239000011115 styrene butadiene Substances 0.000 claims description 11
- 239000000292 calcium oxide Substances 0.000 claims description 10
- 235000012255 calcium oxide Nutrition 0.000 claims description 10
- 230000006835 compression Effects 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 10
- 239000010459 dolomite Substances 0.000 claims description 9
- 229910000514 dolomite Inorganic materials 0.000 claims description 9
- 229920000642 polymer Polymers 0.000 claims description 9
- HHSPVTKDOHQBKF-UHFFFAOYSA-J calcium;magnesium;dicarbonate Chemical compound [Mg+2].[Ca+2].[O-]C([O-])=O.[O-]C([O-])=O HHSPVTKDOHQBKF-UHFFFAOYSA-J 0.000 claims description 8
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 7
- 230000002441 reversible effect Effects 0.000 claims description 7
- 206010040844 Skin exfoliation Diseases 0.000 claims description 6
- ARUVKPQLZAKDPS-UHFFFAOYSA-L copper(II) sulfate Chemical compound [Cu+2].[O-][S+2]([O-])([O-])[O-] ARUVKPQLZAKDPS-UHFFFAOYSA-L 0.000 claims description 6
- LRCFXGAMWKDGLA-UHFFFAOYSA-N dioxosilane;hydrate Chemical compound O.O=[Si]=O LRCFXGAMWKDGLA-UHFFFAOYSA-N 0.000 claims description 6
- 239000011521 glass Substances 0.000 claims description 6
- 238000002360 preparation method Methods 0.000 claims description 6
- 230000000977 initiatory effect Effects 0.000 claims description 5
- 239000010453 quartz Substances 0.000 claims description 5
- 238000005520 cutting process Methods 0.000 claims description 4
- 150000001879 copper Chemical class 0.000 claims description 3
- 239000003171 wood protecting agent Substances 0.000 claims description 3
- 230000010006 flight Effects 0.000 claims description 2
- 235000021067 refined food Nutrition 0.000 claims 2
- 239000004568 cement Substances 0.000 abstract description 9
- 235000008733 Citrus aurantifolia Nutrition 0.000 abstract description 6
- 235000011941 Tilia x europaea Nutrition 0.000 abstract description 6
- 239000004571 lime Substances 0.000 abstract description 6
- 239000000463 material Substances 0.000 description 20
- 239000003795 chemical substances by application Substances 0.000 description 19
- 230000008569 process Effects 0.000 description 16
- 239000000047 product Substances 0.000 description 15
- 239000004576 sand Substances 0.000 description 8
- 238000005406 washing Methods 0.000 description 8
- 235000012239 silicon dioxide Nutrition 0.000 description 7
- -1 crushed stone) Chemical compound 0.000 description 6
- 230000001419 dependent effect Effects 0.000 description 5
- 238000000227 grinding Methods 0.000 description 5
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 230000009471 action Effects 0.000 description 4
- 210000000988 bone and bone Anatomy 0.000 description 4
- 229910002026 crystalline silica Inorganic materials 0.000 description 4
- 230000003247 decreasing effect Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 230000009969 flowable effect Effects 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 239000004575 stone Substances 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000004806 packaging method and process Methods 0.000 description 3
- 239000011236 particulate material Substances 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 239000002023 wood Substances 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 2
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- 235000019687 Lamb Nutrition 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical group CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 239000003599 detergent Substances 0.000 description 2
- 235000013399 edible fruits Nutrition 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 235000013312 flour Nutrition 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 235000021190 leftovers Nutrition 0.000 description 2
- 230000033001 locomotion Effects 0.000 description 2
- ZLNQQNXFFQJAID-UHFFFAOYSA-L magnesium carbonate Chemical compound [Mg+2].[O-]C([O-])=O ZLNQQNXFFQJAID-UHFFFAOYSA-L 0.000 description 2
- 239000001095 magnesium carbonate Substances 0.000 description 2
- 229910000021 magnesium carbonate Inorganic materials 0.000 description 2
- 239000000123 paper Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000003755 preservative agent Substances 0.000 description 2
- 230000004044 response Effects 0.000 description 2
- HIEHAIZHJZLEPQ-UHFFFAOYSA-M sodium;naphthalene-1-sulfonate Chemical compound [Na+].C1=CC=C2C(S(=O)(=O)[O-])=CC=CC2=C1 HIEHAIZHJZLEPQ-UHFFFAOYSA-M 0.000 description 2
- HHVJDKXLUXCHRW-LBPRGKRZSA-N (2,5-dioxopyrrolidin-1-yl) (2s)-2-methoxy-2-phenylacetate Chemical compound O=C([C@@H](OC)C=1C=CC=CC=1)ON1C(=O)CCC1=O HHVJDKXLUXCHRW-LBPRGKRZSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 208000035143 Bacterial infection Diseases 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- 241000700159 Rattus Species 0.000 description 1
- 235000002595 Solanum tuberosum Nutrition 0.000 description 1
- 244000061456 Solanum tuberosum Species 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 241000607479 Yersinia pestis Species 0.000 description 1
- 230000003213 activating effect Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000001580 bacterial effect Effects 0.000 description 1
- 208000022362 bacterial infectious disease Diseases 0.000 description 1
- 235000008429 bread Nutrition 0.000 description 1
- 235000012813 breadcrumbs Nutrition 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 235000021438 curry Nutrition 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 239000011440 grout Substances 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 231100000206 health hazard Toxicity 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 208000015181 infectious disease Diseases 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000002955 isolation Methods 0.000 description 1
- 230000002147 killing effect Effects 0.000 description 1
- 235000012054 meals Nutrition 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000000813 microbial effect Effects 0.000 description 1
- 239000010812 mixed waste Substances 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 235000014594 pastries Nutrition 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 235000021395 porridge Nutrition 0.000 description 1
- 235000012015 potatoes Nutrition 0.000 description 1
- 244000144977 poultry Species 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 230000002829 reductive effect Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
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- 239000007921 spray Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000007723 transport mechanism Effects 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 235000013618 yogurt Nutrition 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B18/02—Agglomerated materials, e.g. artificial aggregates
- C04B18/021—Agglomerated materials, e.g. artificial aggregates agglomerated by a mineral binder, e.g. cement
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/60—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis
- B01F27/72—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a horizontal or inclined axis with helices or sections of helices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/80—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis
- B01F27/90—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers rotating about a substantially vertical axis with paddles or arms
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B03—SEPARATION OF SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS; MAGNETIC OR ELECTROSTATIC SEPARATION OF SOLID MATERIALS FROM SOLID MATERIALS OR FLUIDS; SEPARATION BY HIGH-VOLTAGE ELECTRIC FIELDS
- B03B—SEPARATING SOLID MATERIALS USING LIQUIDS OR USING PNEUMATIC TABLES OR JIGS
- B03B9/00—General arrangement of separating plant, e.g. flow sheets
- B03B9/06—General arrangement of separating plant, e.g. flow sheets specially adapted for refuse
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
- B09B3/20—Agglomeration, binding or encapsulation of solid waste
- B09B3/25—Agglomeration, binding or encapsulation of solid waste using mineral binders or matrix
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
- B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
- B09B5/00—Operations not covered by a single other subclass or by a single other group in this subclass
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/12—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using pressing worms or screws co-operating with a permeable casing
- B30B9/125—Control arrangements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
- B01F27/05—Stirrers
- B01F27/11—Stirrers characterised by the configuration of the stirrers
- B01F27/112—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades
- B01F27/1123—Stirrers characterised by the configuration of the stirrers with arms, paddles, vanes or blades sickle-shaped, i.e. curved in at least one direction
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00474—Uses not provided for elsewhere in C04B2111/00
- C04B2111/00767—Uses not provided for elsewhere in C04B2111/00 for waste stabilisation purposes
- C04B2111/00775—Uses not provided for elsewhere in C04B2111/00 for waste stabilisation purposes the composition being used as waste barriers or the like, e.g. compositions used for waste disposal purposes only, but not containing the waste itself
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Environmental & Geological Engineering (AREA)
- Mechanical Engineering (AREA)
- Civil Engineering (AREA)
- Ceramic Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
An apparatus for processing food waste at the premises of a kitchen comprises an inlet 12 for receiving the waste, a hopper 80 containing drying agent, a feed mechanism 86 for dispensing the drying agent, a comminuter 46,48 to comminute the received waste to provide comminuted waste, a dewatering device to dewater the comminuted waste to produce dewatered comminuted waste, a compressor to compress the dewatered comminuted waste to produce compressed waste, a mixer 88for mixing the compressed waste with drying agent delivered from the hopper to the mixer by the feed mechanism and an outlet to provide processed waste for collection. Ideally, the drying agent is a powder and may be cement, silica, lime or mortar. The comminuter preferably comprises a pair of contra-rotating blades or knives. The dewaterer and compressor comprise an Archimedean screw conveyor 608 in which the gap between the screw and the housing decreases in the compressor section. A method of processing food waste at premises of the kitchen comprises receiving the waste, comminuting the received waste to provide comminuted waste, dewatering the comminuted waste to provide dewatered waste, compressing the dewatered waste to produce compressed waste and mixing the compressed waste with a drying agent.
Description
A method of and apparatus for treating waste and a waste product The present invention relates to a method of and apparatus for treating waste, in particular food waste, for example in a domestic kitchen or in an industrial or commercial kitchen or restaurant.
Such food waste may be cooked or uncooked food and could be for example leftovers from cooked meals, food left on plates, or waste from food preparation.
The collection and disposal of kitchen waste poses an increasing problem. Such waste is commonly periodically collected by local refuse services and is disposed of by incineration or landfill.
Various proposals have been made for handling collected waste. As an example, US 5,302,331 describes a process in which a wide range of collected waste materials including leftover foodstuffs are pulverised using a hammer mill comprising a rotatable drum and steel blades rotating within the drum. The powdered garbage is then removed from the drum and transferred to a mixing container where it is slurried by adding water. Bacterial growth is inhibited by adding a biological fixing agent such as lime, grout, wood putty, adhesives, gypsum, or Portland cement, e.g. a mixture of lime, Portland cement and sand. The slurried mixture may be cast in moulds to set as blocks.
Wilatever processing may be carried out after collection, whilst awaiting collection, the unprocessed waste is liable to attract vermin and to degrade producing unpleasant odours and potentially a health hazard.
Embodiments of the present invention provide for the processing of kitchen or restaurant waste, in particular food waste, in situ at the location of the kitchen or restaurant.
Embodiments of the present invention provide for the processing of kitchen waste on a scale convenient for use by a householder or a small commercial establishment such as a restaurant or hotel so enabling them to treat their own waste and removing the need to store untreated waste for collection.
Embodiments of the invention provide a method of processing kitchen or food waste, the method comprising processing the waste at the premises at which it was generated using apparatus that comminutes received waste to provide comminuted waste, dewaters the comminuted waste to provide dewatered waste, compresses the dewatered comminuted waste and provides processed waste which comprises spongy granulate material, for storage, collection or other disposal.
Optionally the method further comprises the apparatus mixing the compressed waste with a powder to inhibit bacterial infection prior to providing the processed waste.
In an embodiment, a method further comprises collecting processed waste from a plurality of premises and disposing of the collected processed waste.
Disposing may comprise transporting the processed waste to a processing facility. As another possibility, the processed waste may be transported to a waste disposal location for disposal, for
example as landfill.
An embodiment of the invention provides a method for treating kitchen waste to stabilise the waste, pending collection, in the form of waste granules, comprising comminuting the waste to provide comminuted waste, dewatering the comminuted waste to provide dewatered waste, compressing the dewatered waste to produce compressed waste, and mixing the compressed waste with a powder, for example cementitious powder, to form waste granules.
Embodiments of the present invention provide processed waste that is stable, rot free, essentially odour free and not attractive to or edible by pests such as rats. As such, the processed waste does not need to be collected frequently. Thus, waste collections can be decreased in frequency down to any desired level, for instance to once every four weeks.
Embodiments of the present invention provide apparatus for receiving domestic or catering industry kitchen waste comprising food waste and converting the same to a dry, rot resistant, granular form.
The granular product is stable, dry and easily storable to await collection and subsequent disposal by a collecting authority.
Embodiments of the present invention provide apparatus for batch processing kitchen waste comprising food waste, the apparatus comprising an inlet for receiving food waste, a comminuter or comminution device to comminute received waste to provide comminuted waste, a dewaterer or dewatering device to dewater comminuted waste to provide dewatered waste, and a compressor to compress the dewatered waste to produce compressed waste. Optionally a delivery device may be provided to deliver powder to be mixed with the compressed waste by a mixer to form waste granules.
The waste inlet may communicate with a hopper having an outlet communicating with the comminuter by a door mechanism. The inlet may have a lid moveable between a closed position and an open position and the door mechanism and the lid may be interlocked such that the door mechanism opens to release food waste to pass out of the door mechanism to reach the comminuter only when the lid is in the closed position and such that the lid is openable to allow a user to add food waste into the hopper only when the door mechanism is closed.
The comminuter may comprise at least a pair of contra-rotatable driven knife or blade bearing shafts defining a nip through which the waste is forced. The effect of the choppinglslicing action of the knives may be to reduce the waste to particles of not more than 4mm in their largest dimension, preferably not more than 2mm.
In an embodiment, a receiving chamber is provided to receive comminuted waste and to transfer the comminuted waste to the dewaterer. The receiving chamber may have a driven stirring member for stirring the comminuted waste and displacing the waste into the dewaterer.
The driven stirring member may be shaped to urge comminuted waste to enter the dewaterer or dewatering device. As an example, the driven stirring member may have blades having a chord which is inclined to the horizontal with the leading edge of each blade being above its trailing edge.
The dewaterer may comprise an Archimedean screw in a screw housing, the screw housing having an inlet for comminuted waste at a upstream location and an outlet for dewatered waste at a downstream location, and ports or apertures along the length of the housing between the inlet and the outlet allowing water egress therefrom. The pitch, outer diameter and core diameter of this screw may each be constant, so that the waste is not substantially compressed at this point.
Optionally the pitch may decrease progressively or the diameter of the core may increase progressively to impose a greater degree of compression, although the main purpose of this stage is dewatering rather than compression.
The compressor may comprise an Archimedean screw having a screw flight helically arranged over a core having a diameter that increases, in an example progressively expands, from an inlet end to an outlet end of the screw. As another possibility or additionally, the Archimedean screw may have a screw pitch decreasing from the inlet end to the outlet end, although decreasing the screw pitch may reduce the ability of the screw to convey material. The pressure applied during the compression process and the heat generated by friction during the compression process assist the drying of the material being processed and may contribute to sterilising the waste by killing bacteria. If desired, a heat source could be provided to assist drying.
The compressor may have a housing comprising two hinged shells to provide access for cleaning by cleaning fluid and perhaps also to allow for relief of excess pressure caused by an incompressible object inadvertently passing through this part of the machine.
In an embodiment, the dewaterer comprises a dewatering Archimedean screw running in a screw housing having a screw flight around a cylindrical core, the compressor comprises a compressing Archimedean screw having a screw flight around a core, where the two cores are longitudinally connected one to the other or are unitary or integral.
In an embodiment, the apparatus comprises a hopper to contain an agent to aid the drying of the material being processed and a feed mechanism for dispensing the drying agent from the hopper for mixing with the compressed waste.
The agent will generally be a powder or fine granular material and may be any material that is acceptable from health and safety and environmental grounds, that is a material suitable for processing within the apparatus and that facilitates drying of the waste material being processed to produce granular or particulate processed output that can, for example, be stored for a number of weeks awaiting collection.
In an example, the agent may be or comprise a material, such as lime or cement that, when mixed with the material being processed may, dependent upon the moisture content of the material being processed, cause an exothermic reaction, generating heat which may assist the drying of the material being processed. Any suitable form of cement may be used.
The agent may comprise or contain a grinding agent that assists the mixing process and may assist the production of a granular or particulate processed waste output. Examples of grinding agents are relatively hard relatively chemically inert particulate materials such as crushed silica, crushed stone and/or sand.
The agent may comprise or contain a binding agent to assist the production of a granular or particulate processed waste output.
In an example, the agent may comprise at least one of a cement, for example Portland cement, quick lime and finely divided silica or a hydraulic mortar mix.
In an example, the agent may be a hydraulic mortar mix that may comprise silica (which may be crystalline silica, e.g. crushed stone), hydrated lime (CaOH2), and calcium magnesium carbonate (e.g. Dolomite), optionally with some polymer latexsuch asstyrene butadiene latex.
In an example, the agent may be or may comprise, by weight %, crushed quartz 60%, hydrated lime 30%, SBR latex 5%, and Dolomite 5%.
As another possibility, the agent may contain a cement, in an example Portland cement. It may further contain quick lime. It may further comprise fine aggregate such as fine sand, suitably fine silica sand.
One suitable, Portland cement based, cementitious powder is glass block mortar (GBM). A typical GBM contains, by weight %, 50-65% crystalline silica, 20-32% Portland cement, 0-5% latex polymer, 0-5% dolomite (or other calcium carbonate, magnesium carbonate or a mixture thereof) and 0-1% detergent, e.g. sodium naphthalene sulfonate. Suitably the latex polymer is vinyl acetate, SBR (styrene-butadiene) or acrylate.
A fungicide may be added at an appropriate stage in the processing of the waste material. The drying agent may optionally comprise a fungicide which may be added as a dry powder, for example added with or as part of the drying agent, or liquid fungicide which could be added to the original waste or at another stage prior to addition to the drying agent. Copper sulphate (or other copper salt) is a preferred fungicide, to be used as a dry powder or, less preferably, in solution.
Other possible fungicides include wood preservatives.
Where the drying agent is used, then in an embodiment an aim is for the dewaterer to output material having a water content suitable to the amount of drying agent to be used such that suitably dry granules will be produced at the end of the process.
The mixer may comprise a mixing chamber containing at least one rotatable blade member.
The apparatus may include functionality to execute a cleaning cycle, which, in response to initiation of a cleaning cycle, causes cleaning liquid to be passed through one or more of the dewaterer, the compressor and the comminuter, and spent cleaning fluid to be discharged via an outlet drain orifice.
The dewaterer and compressor may comprise screw conveyors that may be run in a reverse direction during a cleaning cycle.
The apparatus may comprise one or more sensors to enable automatic initiation of a cleaning cycle when the presence of waste in the apparatus is no longer detected after waste has been processed.
A valve may be provided between an outlet of the compressor and the mixer which valve is moveable between an open position wherein the outlet communicates with the mixing chamber and a closed position wherein the outlet is closed off from the mixing chamber. Isolation of the mixer from the upstream parts of the path taken by the waste enables those parts to be washed whilst the mixer is kept dry.
Embodiments of the invention will now be described by way of example with reference to the accompanying drawings, in which: Figure 1 shows a functional block diagram of apparatus embodying the invention; Figure 2 shows a flow chart illustrating a process embodying the invention; Figure 3 shows a functional diagram of one example of apparatus embodying the invention; Figure 4 shows a perspective view of an example of a receiving chamber of apparatus embodying the invention; Figure 5 shows a perspective view, in an open position, of a shroud of a screw conveyor of a compressor of an apparatus embodying the invention; Figure 6 shows a photograph of a sample of material entering a mixing chamber of apparatus embodying the invention; Figure 7 shows a photograph of a sample of processed waste output by apparatus embodying the invention; and FigureS shows a photograph of a sample of processed waste output by apparatus embodying the invention where the drying agent is omitted from the processing.
Referring now to the drawings, Figure 1 shows a functional block diagram of an example of apparatus embodying the invention.
The apparatus is of a size suitable for placement within a domestic, industrial or commercial kitchen. Where the apparatus is designed to handle domestic food waste then it may be 300 mm (millimetres) wide and 500 mm deep and designed to fit under a normal kitchen worktop. As another possibility, the apparatus may be of a size similar to a dishwasher or washing machine (for example having a 500mm by 500 mm or 600mm by 600mm footprint). When the apparatus is for use in an industrial or commercial selling then it may be larger.
As shown in Figure 1, the apparatus has a housing 10 having a waste inlet 120 to allow a user to charge a waste receiver 140 mounted within the housing with kitchen waste, in particular food waste, for example left over cooked or uncooked food, cooked or uncooked food remaining on plates and food scraps or peelings produced during food preparation.
The waste receiver 140 is coupled to supply received waste to a comminuter 200 to produce comminuted waste. The comminuter 200 is coupled to supply comminuted waste to a dewaterer 500. The dewaterer 500 is coupled to output dewatered waste material to a compressor 501 that is provided to compress the dewatered comminuted waste and to supply compressed dewatered comminuted waste. The compressed dewatered comminuted waste may be supplied directly to an outlet 920 of the apparatus.
The apparatus has a powder receiver 801 coupled to receive a drying agent, generally a powder, from a powder inlet 800 and to supply the drying agent to a mixer 880 provided to mix the compressed dewatered comminuted with powder prior to output. The purpose of the drying agent is to enhance the dryness and thus the lifespan of the resultant processed waste product, enabling it to be stored for collection.
It will of course be appreciated that Figure 1 is intended simply to represent the functionality provided and the functional components shown in Figure 1 need not necessarily in reality be separate components. As an example the dewaterer and compressor may be provided by the same component.
In operation as illustrated by Figure 2, a user places food waste (as explained above) into the waste receiver 140 (Si). The waste may be stored there temporarily, with further waste being added from time to time. The user also charges the powder receiver 801 with the drying agent.
When the apparatus is activated by the user, food waste is supplied from the waste receiver 140 to the comminuter 200 and the comminuter is driven to chop, shred and grind the food waste to particles or granules with a size and consistency similar to that of bread crumbs (52). The comminuter may comprise one or more shredding blades.
The comminuted waste passes to the dewaterer 500 where it is dewatered and somewhat compressed (S3) before being transferred to the compressor 501 (S4). The dewaterer 500 may be designed so that for example, depending upon the original water content, 50-70% of the weight of the waste is removed as liquid water. The compressor may be designed to put the waste under high pressure, for example in the range 5MPa -35MPa or higher, for example 400MPa and may subject it to frictional heating, resulting in a temperature rise which may be, for example, 7-10 degrees Celsius, depending upon the food waste being processed. The waste may be heated (for example by heat exchange with a hot water supply). In an example the dewaterer and compressor may be provided by respective sections of a screw conveyor with, at least in the high pressure section, the diameter of the core increasing and/or the pitch of the conveyor screw decreasing, for example continuously, toward its rearward end, that is in the direction in which the waste is being transferred, so as to compress the waste as it is transported by the screw conveyor.
The comminuted, dewatered and compressed waste may now have a paste-like consistency and a water content of typically about 30%, preferably 25%, by weight.
Where provided, the agent will generally be a powder or fine granular material and may be any material that is acceptable from health and safety and environmental grounds, that is suitable for processing within the apparatus and that facilitates drying of the waste material being processed to produce granular or particulate processed output that can, for example, be stored for a number of weeks awaiting collection.
Where a powder is supplied, the powder from the powder receiver 801 and compressed dewatered comminuted waste output from the compressor are mixed by the mixer (S6) and supplied to the output (S7). In an example, the powder may be supplied to provide a ratio, by volume percent, of to 35% waste to powder, depending upon the food type. For a domestic apparatus, the powder receiver may hold about 1 Kg (Kilogramme) of drying agent, which may be sufficient to process an average family's food waste for one week. The mixer also acts further to slice or shred the waste material.
In an example, the agent may be or comprise a material, such as lime or cement that, when mixed with the waste being processed may, dependent upon the moisture content of the waste being processed, cause an exothermic reaction, generating heat which may assist the drying of the waste being processed. Any suitable form of cement may be used.
The agent may comprise or contain a grinding agent that assists the mixing process and may assist the production of a granular or particulate processed waste output. Examples of grinding agents are relatively hard, relatively chemically inert particulate materials such as at least one of crushed silica, crushed stone and sand. The agent may comprise or contain a binding agent to assist the production of a granular or particulate processed waste output.
As an example the powder may be an alkaline or lime-based powder such as for example a cementitious powder, quick lime, a hydraulic mortar mix. An example of a hydraulic mortar mix may comprise silica (which may be crystalline silica, e.g. crushed stone), hydrated lime (CaOH2), and calcium magnesium carbonate (e.g. Dolomite), optionally with some polymer latex such as styrene butadiene latex. In a specific example the hydraulic mortar may comprise, by weight %, crushed quartz 60%, hydrated lime 30%, SBR latex 5%, and Dolomite 5%.
In an example a cementitious powder may comprise Portland cement. A cementitious powder may also contain one or both of quick lime and a fine aggregate such as fine sand, suitably fine silica sand.
An example of a suitable Portland cement based cementitious powder is glass block mortar (GBM).
A typical GBM contains, by weight %, 50-65% crystalline silica, 20-32% Portland cement, 0-5% latex polymer, 0-5% dolomite (or other calcium carbonate, magnesium carbonate or a mixture thereof) and 0-1% detergent, e.g. sodium naphthalene sulfonate. The latex polymer may be vinyl acetate, SBR (styrene-butadiene) or acrylate.
After mixing, the waste and powder will have formed processed waste output comprising particles of around 1-2mm in size which are quite dry and so form a flowable coarse powder which is provided to the outlet 920. Where the powder comprises a cement andlor quicklime, the chemical reaction between the powder and the damp food waste generates heat which accelerates the drying time, compacting increasing with temperature, resulting in a particulate material which progressively sets or hardens (akin to cement going off') to produce the flowable coarse powder.
The outlet 920 may comprise a chute 94 and may deliver the flowable coarse powder into a bag, suitably of paper or other biodegradable material, or other receptacle. For domestic use, the bag may be of similar size to a vacuum cleaner bag.
The processed waste output by the apparatus may be set aside for future disposal as it is quite odourless and unaffected by becoming wet. The processed waste can therefore be stored without difficulty to await collection.
A fungicide may be added at an appropriate stage in the processing of the waste material. The agent may optionally comprise a fungicide, which may be added as a dry powder, for example added with or as part of the drying agent, or a liquid fungicide could be added to the original waste or at another stage prior to addition to the drying agent. Copper sulphate (or other copper salt) is a preferred fungicide, to be used as a dry powder or, less preferably, in solution. Other possible fungicides include wood preservatives.
An example of a food waste treatment apparatus according to the invention will now be described with reference to Figures 3, 4 and 5, in which Figure 3 shows a functional diagram illustrating examples of the various functional components of the apparatus, how they cooperate and how the various materials pass through the apparatus. In this example, the apparatus is designed to receive food waste and to process it through six stages to produce as a final product a dry granular material.
WASTE RECEPTION
In this example, the waste inlet is in the form of a user-openable door 12 of the housing 10. The door 12 may be for instance hinged or slideable for opening. Door 12 gives access to the waste receiver which in this example is a hopper 14.
The hopper 14 has hinged or pivotable wall members 22 (only one being visible in Figure 3) that are movable between a closed position in which the hopper retains waste and an open position in which the hopper discharges waste to the comminuter.
The pivotable side wall members 20 are pivotable about axes 24a by any appropriate mechanism (not shown), in this example by means of a crank mechanism, coupled to a drive mechanism 180 (see below) of the apparatus.
The sidewall members 20 of the hopper 14 are thus moveable between a first, downwardly closed, position and a second, downwardly open, position. Thus when the side wall members 20 are in the second downwardly open position waste product is released from the hopper into the comminuter whilst when the side wall members 20 are in the first downwardly closed position waste, the wall members press down on food waste that is below them to facilitate comminution.
An interlock mechanism (not shown) ensures that the lid or door 12 is locked before the hopper 14 is opened to discharge waste into the comminuter or comminution device.
COMMINUTION DEVICE
In this example the comminuter or comminution device has two parallel, contra-rotating shafts 44 and 46 below the hopper side wall members 20. Each shaft 44, 46 bears a stack of bladed wheels 48 configured to rotate with their shaft 44, 46. For example, the bladed wheels 48 may be keyed for rotation with their respective shaft 44, 46. As another possibility, the shafts 44 may have a non-circular cross-section, e.g. octagonal. The wheels 48 of the two shafts 44 and 46 are intermeshed and rotate so as to draw waste down between the shafts 44 and 46. Each bladed wheel 48 bears knife teeth (for example eight) which may, as an example, be shaped such that the distal end of each tooth lies rotationally behind the radius bisecting the root of the tooth, the leading edge of the tooth being convexly curved for a scything action through the food waste. The contra-rotatable shafts 44 and 46 define a nip through which in operation the waste is forced. The effect of the chopping/slicing action of the knives may be to reduce the waste to particles of not more than 4mm in their largest dimension, preferably not more than 2mm.
In this example, a receiving chamber 50 is provided below the bladed wheels 48 to receive comminuted waste and to transfer the comminuted waste to the dewaterer. The receiving chamber may have a driven stirring member for stirring the comminuted waste and displacing the waste into the dewaterer.
Figure 4 illustrates an example of the receiving chamber 50. In the example shown in Figure 4, the receiving chamber may have a cylindrical sidewall 52 and a floor or bottom wall 54. A rotatable shaft 62 driveable by the drive 180, runs front to back through the chamber 50 and operates a gearbox 64 at the central axis of the chamber 50 to drive a downwardly extending shaft 66 carrying a pair of outwardly (radially of the chamber 50 where it is cylindrical) extending stirring arms 68 which lie just above the bottom wall 54 of the chamber 50.
The stirring arms 68 may be shaped to urge comminuted waste to enter the dewaterer. As an example, the driven stirring member may have blades having a chord which is inclined to the horizontal with the leading edge of each blade being above its trailing edge.
DEWATERER AND COMPRESSOR
The bottom wall 54 of the receiving chamber 50 has a hemi-cylindrical bulge 56 extending across its width (right to left in Figure 3) at the top of which is an opening 58 (which may be rectangular).
Below chamber 50 there runs, extending rearwardly (to the left in Figure 3), a first, low pressure stage 60a of a two stage first Archimedean screw conveyor 60. The first, low pressure stage 60a comprises a screw member running in a cylindrical housing which has a top opening 59 therein mated to the rectangular opening 58. A cylindrical housing (or shroud) 600 of the first stage of the screw conveyor is perforated with holes 63 on its underside to allow water to be squeezed out of the waste to dewater the waste. In this example the holes are 2mm holes although other size holes may be used provided that they enable water to exit but not the waste. To the right (in Figure 3) of the perforated region of the cylindrical housing of the first stage of the screw conveyor and of the top opening 59 therein is a downward facing opening 61 (which in an example may be rectangular) in the housing. This opening 61 is for use during a cleaning operation and is for allowing egress of material in the conveyor when the screw is run in reverse to drive such material towards the opening 61.
The pitch, outer diameter and core diameter of this first, low pressure stage 60a of the first Archimedean screw conveyor 60 may each be constant, so that the waste is not substantially compressed at this point. Optionally, however, the pitch may decrease progressively and/or the diameter of the core may increase progressively to impose a greater degree of compression, although the main purpose of this stage is dewatering rather than compression.
Rearward (to the left in Figure 3) of the chamber 50, a second stage 60B of the screw conveyor 60 is formed as a high-pressure region. In the first stage 60A of the screw conveyor, the screw comprises a constant pitch helical flight on a constant diameter core. In the second stage 60B, the screw comprises a core of progressively expanding (rearwardly) cross section bearing a constant pitch helical screw flight so as to facilitate compression. In a domestic sized unit, the constant diameter core of the first stage of the screw conveyor may be for instance 120mm in length whilst in the second stage of the screw conveyor, the progressively expanding core may have a length of 250mm. The core may have a diameter of 15mm over its constant diameter part, expanding in the second section to 30mm. The overall diameter of the screw may be 35mm. The high-pressure region may have a taper and operational speed such as to produce a pressure of 4,000 bar (58,000 psi). The moisture or water content at this stage may be 25% by weight.
In the second stage 60B of the screw conveyor, the screw is contained within a shroud 70 which may be opened for cleaning purposes. Figure 5 shows an example of the shroud 70, in an open position. As shown in Figure 5, the shroud 70 is formed by two hollow hemi-cylindrical shells 72, 74 carried by respective arms 76 which are hinged for movement about a shaft 78 extending parallel to and above the shroud 70. The shells are moveable between a first, closed, position in which they form the shroud 70 enclosing the screw, and a second position shown in Figure 5 in which the screw is accessible for cleaning. In an intermediate position, not shown, pressure within the shroud is released and any trapped solid items can be downwardly expelled as described in more detail below.
The hinged shells 72, 74 thus provide access for cleaning by cleaning fluid and may also allow for relief of excess pressure caused by an incompressible object inadvertently passing through this part of the machine.
The shroud 70 of the second stage of the screw conveyor is itself contained within a cylindrical washing chamber 170 to which cleaning fluid is pumped as described below.
POWDER RECEIVER
In this example, the powder receiver is a powder hopper 80 disposed to the rear of the rear wall of the hopper 14. The powder hopper 80 has at its top opening a user-openable door 82, which may be, for example, hinged or sliding in action. From the base of the powder hopper 80 extends downwardly a powder chute 84 which communicates with an upwardly facing opening in a shroud of a second Archimedean screw conveyor 86.
MIXER
Behind the second stage of the first screw conveyor lies a cylindrical mixing chamber 88 into the top of which the second screw conveyor 86 empties via a port 90 so that dewatered, comminuted food waste from the first screw conveyor 60 and the powder from the hopper 80 meet and are mixed by a large diameter mixing screw 89 and conveyed to the rear of the mixing chamber.
OUTLET
Mixed waste exits the mixing chamber 88 via a port 92 in the base thereof and falls into a tapering chute 94 from which it is driven by a fourth screw conveyor 96 forwardly (to the right in Figure 3) to exit via a mouth 98 into a bag 101 retained in a bag tray 100 which can be removed from the apparatus by sliding out of a front of the housing 10. The tray 100 may have a heat conductive (e.g. metal) base which may assist the drying process.
CLEANING
Below the first stage of the first screw conveyor there is a filter tray 102 having over its top opening a mesh filter 104 which may for example be made of wire or plastics. The tray 102 is slideable out of the front of the apparatus for cleaning.
Provision is made for a cleaning cycle for washing through those parts of the apparatus that encounter wet food waste whilst keeping dry the parts of the apparatus through which pass the powder from hopper 80. Thus, the apparatus may conceptually be divided into a wet part' and a dry part'. The dry part' is the part through which the powder passes and comprises the powder hopper 80, the screw conveyor 86, the mixing chamber 88, and the path therefrom to the collecting bag 101. The wet part' comprises the whole path of the food waste up to its mixing with the powder. Only the wet part' is washed in the cleaning cycle.
A water inlet is provided at 110 to a cleaning pump 112 from which water is directed to a hot water cylinder 150 provided at the rear of the apparatus adjacent the mixing chamber 88. An electrical heater element 152 extends within the hot water cylinder 150. Pipework communicates the hot water cylinder with the spray jets 120 above the sidewalls of the hopper 14 and with the washing chamber 170 that surrounds the conveyor shroud 70. Washing chamber 170 drains into the filter 104 through pipework to a drain hole 170a that exits above the filter 104. A drain 172 extends from the filter tray 102 rearwardly to a discharge sand filter 174 connected via a drain pump 162 to a discharge outlet 176 to be connected to a foul water drainage system. Thus, all the water used in a cleaning cycle ultimately drains via drain 172 to the discharge filter 174 and is ejected by the drain pump 162.
Between the high pressure section 60B of the first screw conveyor within shroud 70 and the mixing chamber 88 is positioned a rotary ball valve 166 operated by a rotatable shaft 168. The valve is operable as a ball valve to prevent cleaning water progressing rearwardly into the dry section of the apparatus (mixing chamber 88).
A cleaning solution container 178 is provided which also has a user openable cover 178a. This feeds cleaning solution to the feed of hot water exiting from the hot water cylinder 150 as it passes through a Venturi 148.
CONTROL SYSTEM
Components of the apparatus are driven by a motor drive mechanism of a control drive system 180. The motor drive mechanism comprises an electric motor coupled to drive the various components via belt drive and gear drive arrangements, as appropriate. In the interests of clarity, these are not shown in Figure 3. As an example, the drive mechanism may have a gearing box with an output shaft which drives a first of the knife or blade bearing shafts 44 and 46, drive being communicated to the other shaft 46 by meshing pinions connecting the two shafts for contra-rotation. The screw conveyors 60, 86, 96 and the mixing chamber screw 89 may be driven by belt drives coupled to the motor. The gearbox 64 is coupled via shaft 62 to the drive motor. Thus, as an example, an internally toothed drive belt (not shown) may connect a sprocket at the opposite end of one of the shafts 44 and 46 to a sprocket on the forward end of the screw member of the Frst screw conveyor whilst another drive belt may take power from the same gearbox to the mixing chamber screw in mixing chamber 88 and to the fourth screw conveyor 96.
In the interests of simplicity, the electrical couplings and sensors of the control system are not shown in Figure 3. Various sensors are provided for detecting whether supplies of powder and cleaning fluid are present and whether the bag in tray 100 is full, and whether the various trays and doors are closed properly. Indicator lights may be provided to inform the user of the status reported by some or all of these sensors. User input devices (switches andlor buttons) for controlling operation of the apparatus are also not shown. It will of course be appreciated that the timing of operation of the components coupled to the motor drive mechanism is controlled by the gearing ratios and belt drive arrangements and that the control system is arranged to ensure that the motor is not operated unless the doors are shut and the hoppers contain sufficient material (waste or powder as the case may be). The control system also may stop operation of the motor and other components in the event of detection (for example by undue load on the motor) of a foreign or unduly large object (such as a piece of cutlery or very large bone) in the screw conveyor 60. In such circumstances, the control system also may be designed to automatically reverse operation of the screw conveyor to eject the unwanted object or to alert a user to enable the user to activate a user input device to reverse operation of the screw conveyor.
The control system may cause a cleaning cycle to be carried out automatically or in response to a user activating a user input device that controls initiation of a cleaning cycle.
The control system may comprise an electromechanical control system or a microprocessor or computer control system, in a manner similar to that of a washing machine or dishwasher.
OPERATION OF THE APPARATUS
In use, the apparatus functions as follows, under the control of the control system and the user. In a first stage, food waste (as explained above) is placed by the user into the hopper 14 and the hopper door 12 is closed. The waste may be stored there temporarily as desired, with further waste being added from time to time. Powder (as explained above) is charged into the powder hopper 80, and cleaning fluid (as explained above) is charged into the cleaning fluid container 178.
When desired, the apparatus is activated by the user. Provided that all safety checks are met, including sensing that the food waste door 12 is closed, the motor 180 drives the hopper sidewalls to pivot to their open position, dropping food waste onto the now rotating knife shafts 44, 46.
In the second stage of the process, the food waste is chopped, shredded and ground by the knife shafts 44, 46 and the bladed wheels 48 they carry and is reduced to particles of about 2mm in size.
Even quite large bones are easily dealt with, but if some object such as cutlery is dropped in by accident, this is sensed as excessive resistance to movement of the main drive motor. In this event, overload of the motor triggers the motor to stop and to reverse. The blades are reversed by reversal of the motor to expel the article, an alarm is given by sound or visible indication and the process is halted. The item can be retrieved from the filter tray 102 having been carried out over the side of the bladed wheels 48 onto the filter 104.
The comminuted waste is dragged down through the nip provided by the bladed shafts 44 and falls into the waste receiving chamber 50 below, where the stirring arms 68 guide the waste through the outlet opening 58 to enter the first, low pressure, section of the first screw conveyor 60.
In the third stage, the waste is driven rearwardly between the screw of the first low pressure section 60A of the first screw conveyor 80 and its covering shroud and is dewatered and somewhat compressed, with liquid exuded from the waste passing through the apertures 63 in the shroud to fall into the filter tray 102 below via the filter 104. Depending on the original water content of the waste, typically 50-70% of the weight of the waste is lost here as liquid water.
From there, the waste is driven rearwardly into the second, high pressure, stage 60B of the first screw conveyor 60. As set out above, in the second stage, the cross-sectional area of the screw conveyor core increases, for example continuously, toward the mixing chamber (altematively or additionally the pitch of the screw conveyor decreases, for example continuously, toward the mixing chamber). This causes compression of the waste and, as a result, the waste is put under high pressure. The pressure in this section can amount to 2SMPa -3SMPa or higher, for example 400MPa (Mega Pascal). This second, high pressure, section 60b may generate heat which may assist in the drying of the waste. This heat could also be utilised to help heat the cleaning water.
The shells 72 and 74 surrounding the screw of the conveyor are of course closed at this stage, but they can be forced open slightly if excessive pressure builds up in the conveyor, e.g. if a non-compressible body makes it this far into the process. If for instance a chip of bone or the like too large to pass through this section with the shells fully closed enters this part of the conveyor, opening the shells by say 1mm will allow it to pass through into the mixing chamber 88 by providing a little extra clearance.
The comminuted waste now has a paste-like consistency and a water or moisture content of typically about 30% by weight, preferably 25% by weight, as it emerges through valve 160 into the mixing chamber 88 into which powder is delivered from the hopper 80. The powder contained in hopper 80 may be any of those mentioned above. As an example, the powder may be a mixture of Portland cement, quick lime and fine silica of the kind conventionally sold as glass block mortar, with an optional addition of a fungicide such as copper sulphate. The waste may be heated during the mixing process by hot water in the hot water cylinder 150.
The mixture of powder and food waste is sliced and mixed in a fifth stage of the process by the thread of the mixing screw 89 in the mixing chamber 88 and is progressively forced rearwards before, in a sixth stage of the process, being forced down through the chute 94, along the last screw conveyor 96, and into a bag, suitably of paper, in the bag tray 100. At this point, the waste and powder will have formed particles of around 1-2mm in size which are quite dry and which progressively set to become a flowable coarse powder. Should the bag fill part way through the process, a full bag sensor (not shown) will cause the control system to stop operation of the apparatus and to alert a user to allow a replacement bag to be fitted.
The bag containing the processed waste can be set aside for future disposal as its contents are quite odourless and are unaffected by becoming wet. The processed waste can therefore be stored without difficulty to await collection.
At the end of the working cycle, when all the waste from the waste hopper 12 has been treated, absence of further waste just upstream of the collection bag is sensed by a sensor (not shown) such as a paddle switch or the like.
Where the waste food hopper 14 has a capacity similar to a large loaf of bread then typically a full hopper of waste may be processed in about 60 seconds.
The control system may cause a wash cycle to be commenced a set time after the end of the working cycle. Of course, if preferred this automatic feature can be omitted and the wash cycle can be manually initiated.
In the wash cycle, water from the hot water tank 150 containing entrained cleaning fluid from the container 178 is pumped to jets 120 in the lid ordoor 12 of the hopper 14 and the control system causes the pivoting sidewalls 20 to open and shut several times (e.g. three times) to allow their undersides to be cleaned. The control system keeps the pivoting sidewalls 20 remain open to allow cleaning of the knife blades on the wheels 48 and the wet food processing zones below them.
The control system will also have caused shells 72, 74 of the shroud in the high-pressure conveyor zone to be opened to enable water to be supplied for cleaning into the washing cylinder 170. It will of course be appreciated that, before a wash cycle is commenced, the control system causes valve (which may be a rotary ball valve) to close to prevent water passing into the dry part' of the apparatus. As show in Figure 3, the cleaning water drains through drain hole 170a into the filter tray 102 above the filter 104. Although not shown in Figure 3, the control system may cause the cleaning water to be recirculated from the filter tray 102 before being pumped out by the drain pump and then cause clean water to be pumped through the wet part' to complete the cleaning cycle.
The control system ensures that user operable lids are locked down during the cleaning process but are released at its end and the valve 160 opened so that the apparatus is then ready again for use. The whole cleaning cycle may last only about 1 minute 40 seconds.
The described apparatus is suitable for installation in a conventional domestic or commercial kitchen in the same way as a washing machine or dishwasher. It is capable of receiving and processing not purely food waste, but essentially everything that might normally be left on a plate, including light food packaging such as yoghurt pots and non-edible portions of foods like fruit peelings and cores. Moreover, it is capable of receiving and dealing with poultry carcasses and bones from carved joints. Whilst the apparatus would successfully receive and pass through materials like cardboard packaging or plastics packaging, this is not desirable because such non-biodegradable materials are able to be recycled usefully. Moreover, although they will pass through the apparatus, they will not inherently contain sufficient water to react properly with the powder described above.
One or more of the screw conveyers may be replaced by other transport mechanisms, such as piston arrangements, and, where appropriate, dewatering and compression may be achieved by other means such as a centrifuge arrangement. Other forms of valves, hoppers and closure mechanisms that provide the same or similar functionality may be used. In the example described above, the hopper 14 has pivoting sidewalls, other suitable mechanisms for enabling discharge of waste from a full hopper onto the contra-rotating knife blades may be used, for example a sliding door arrangement. Also the relative positions and orientations of the components need not necessarily be as described above. Also the bag 101 may be replaced with another form of collection mechanism.
EXAMPLES
Apparatus embodying the invention has been used to process food waste in the form of, for example, a lamb dinner with potatoes and vegetables and a chicken curry. Figures 6, 7 and 8b show processed waste where the waste was a lamb dinner and the proportion of waste food to powder was 25 to 35% by volume waste to powder as described above with the powder being a Portland cement based powder as discussed above. Figure 6 shows a photograph illustrating the output of the compressor (the second stage of the screw conveyor in the example above), that is the input to the mixing chamber 88 whilst Figure 7 shows a photograph illustrating the processed output supplied to the bag 101. The waste output by the compressor has a consistency similar to solidified porridge whilst the actual output of the apparatus is a dry granular material that has a consistency similar to that produced by mixing flour, fat and sugar to produce a topping for a fruit crumble or after mixing flour and fat prior to the addition of water during the making of short crust pastry. Typically the final processed waste has a particle size of about 2mm on average. The colour of the final processed waste product is dependent upon the colour of the "ingredients" (the waste and the powder) but the final processed waste is a dry granular material that is odourless and that can be stored at the site of the kitchen for 4 to 6 weeks or more without the need for refrigeration or cooling, even in summer. Indeed, lifespans of about four months before microbial infection sets in have been achieved.
As described above the drying agent comprises a powder. Drying agents that perhaps would be considered to be granular materials or granulars and may themselves having little or no tendency to clump or which have a slightly larger particle size than perhaps would be usual for a powder may be possibilities and should be considered to fall within the definition of powder as used herein, the requirement being that the powder assists the drying of the comminuted, dewatered and compressed waste and perhaps also its mixing and grinding.
The addition of the powder to the comminuted, dewatered and compressed waste significantly assists in the drying and the achievement of the lifespans mentioned above. Where such lifespans are not required, then the powder may be omitted. Figure 8 shows a photograph illustrating the processed output supplied to the bag 101 when the powder is omitted. It is clear from a comparison of Figures 7 and 8 that omission of the powder results in a processed waste product that has a significantly larger particle size, looking more like a spongy granola than crumble topping, this possibly resulting partly from the higher moisture content causing clumping.
In this specification, unless expressly otherwise indicated, the word or' is used in the sense of an operator that returns a true value when either or both of the stated conditions is met, as opposed to the operator exclusive or' which requires that only one of the conditions is met. The word comprising' is used in the sense of "having" and/or including' rather than to mean necessarily consisting of'. All prior teachings acknowledged above are hereby incorporated by reference. No acknowledgement of any prior published document herein should be taken to be an admission or representation that the teaching thereof was common general knowledge in Australia or elsewhere at the date hereof
THE DISCLOSURE OF THIS APPLICATION ALSO INCLUDES THE FOLLOWING NUMBERED
CLAUSES: 1. A method of processing waste, such as food waste, from a kitchen, the method comprising apparatus on the premises of the kitchen: receiving the waste; comminuting the received waste to provide comminuted waste; dewatering the comminuted waste to provide dewatered waste; compressing the dewatered waste to produce compressed waste; and providing processed waste to await collection.
2. A method according to clause 1, which further comprises mixing the waste with a drying agent, which may be a powder, after compression.
3. A method according to clause 1, which further comprises mixing the compressed waste with a cementitious powder, to form cementitious waste granules, and storing the granules to await collection.
4. A method according to clause 2 or 3, wherein the drying agent or powder comprises at least one of Portland cement, quicklime, finely divided silica, a hydraulic mortar mix.
5. A method according to clause 2 or 3, wherein the drying agent or powder comprises a hydraulic mortar mix comprising silica, hydrated lime, and calcium magnesium carbonate.
6. A method according to clause 2 or 3, wherein the drying agent or powder comprises a hydraulic mortar mix comprising silica, hydrated lime, and calcium magnesium carbonate and a polymer latex such as styrene butadiene latex.
7. A method according to clause 2 or 3, wherein the drying agent or powder comprises crushed quartz 60%, hydrated lime 30%, SBR latex 5%, and Dolomite 5%, by weight.
8. A method according to clause 2 or 3, wherein the drying agent or powder comprises a glass block mortar (GBM).
9. A method according to any of clauses 2 to 8, wherein the drying agent or powder comprises a fungicide.
10. A method according to clause 9, wherein the fungicide comprises copper sulphate, another copper salt, or a wood preservative.
11. A method according to any preceding clause, wherein comminuting the received waste provides particles of about 2mm in size.
12. A method according to any preceding clause, wherein dewatering the comminuted waste results in 50-70% of the weight of the waste being lost as liquid water.
13. A method according to any preceding clause, wherein during compression of the dewatered waste a pressure of at least 25MPa -35MPa is applied to the waste.
14. A method according to any of the preceding clauses, wherein the waste comprises one or more of: food preparation scraps such as cuttings and/or peelings; left over food; food left on plates; cooked food; uncooked food.
15. A method of disposing of waste, such as food waste, from the kitchens of a plurality of premises, the method comprising: collecting processed waste produced by a method in accordance with any of clauses 1 to 14 from the plurality of premises; and disposing of the collected processed waste.
16. A method according to clause 15, wherein disposing comprises transporting the processed waste to a processing facility and incorporating the processed waste into manufactured products at the processing facility or (b) to transporting the processed waste to a waste disposal location.
17. A method for treating kitchen waste to stabilise the waste pending periodic collection in the form of cementitious waste granules, the method comprising comminuting the waste to provide comminuted waste, dewatering the comminuted waste to provide dewatered waste, compressing the dewatered waste to produce compressed waste, and mixing the compressed waste with a drying agent, for example a cementitious powder, to form the cementitious waste granules.
18. A processed waste product, the product comprising comminuted, dewatered and compressed kitchen waste such as food waste in a crumble-like, granular or spongy granular form.
19. A processed waste product according to clause 18, wherein the product further comprises a powder mixed with the kitchen waste.
20. A processed waste product according to clause 19, wherein the powder comprises at least one of Portland cement, quicklime, finely divided silica, a hydraulic mortar mix.
21. A processed waste product according to clause 19 or 20, wherein the powder comprises a fungicide.
22. A processed waste product according to any of clauses 19 to 21, wherein the waste comprises one or more of food preparation scraps such as cuttings and/or peelings; left over food; food left on plates; cooked food; uncooked food.
23. A processed waste product according to any of clauses 19 to 22, wherein the granules are about 1-2mm granules.
24. Apparatus for processing kitchen waste comprising food waste at the premises of the kitchen, the apparatus comprising: an inlet for receiving the kitchen waste; a comminuterto comminute the received waste to provide comminuted waste; a dewatering device to dewater the comminuted waste to provide dewatered comminuted waste; a compressor to compress the dewatered comminuted waste; and an outlet to provide processed waste ready for collection.
25. Apparatus according to clause 24, further comprising: a device to provide a drying agent to be mixed with the compressed waste and a mixer to mix the compressed waste with drying agent so that in use the processed waste is provided as cementitious waste granules.
26. Apparatus according to clause 24 or 25, wherein the inlet has a lid moveable between a closed position and an open position and the inlet communicates with a hopper having an outlet, the hopper outlet communicating with the comminuter by a door mechanism, and wherein the door mechanism and the lid are interlocked such that the door mechanism opens to supply food waste to the comminuter only when the lid is in the closed position and such that the lid is openable to allow a user to add food waste into the hopper only when the door mechanism is closed.
27. Apparatus as set out in any of clauses 24 to 26, wherein the comminuter comprises at least a pair of contra-rotating driven knife or blade bearing shafts defining a nip through which waste is forced.
28. Apparatus as set out in any of clauses 24 to 27, wherein the comminuter comprises a receiving chamber to transfer waste to the dewatering device, the receiving chamber having a stirring member for stirring and/or guiding the waste.
29. Apparatus as set out in clause 28, wherein the stirring member is shaped to urge waste into the dewatering device.
30. Apparatus as set out in any of clauses 24 to 29, wherein the dewatering device comprises an Archimedean screw having a housing with apertures for egress of water.
31. Apparatus as set out in any of clauses 24 to 30, wherein the compressor comprises an Archimedean screw having a screw flight and a core and wherein at least one of: the core increases in diameter from an inlet to an outlet of the screw; and the pitch of the screw decreases from the inlet to the outlet.
32. Apparatus as set out in clause 31, wherein the compressor has a housing surrounding the screw, the housing comprising hinged shells arranged to open to allow cleaning.
33. Apparatus as set out in any of clauses 24 to 29, wherein the dewatering device and the compressor comprise Archimedean screws having screw flights arranged on cores that are coupled to one to the other or are integral or unitary.
34. Apparatus as set out in clause 25 or any of clauses 26 to 33 when dependent on clause 25, further comprising a hopper to contain the drying agent and a feed mechanism for dispensing the drying agent from the hopper for delivery to mix with the compressed waste.
35. Apparatus as set out in clause 25 or any of clauses 26 to 34 when dependent on clause 25, wherein the mixer comprises a mixing chamber containing at least one rotatable blade member.
36. Apparatus as set out in any of clauses 24 to 35, wherein a valve is provided at an outlet of the compressor, which valve is moveable between an open position and a closed position.
37. Apparatus as set out in any of clauses 24 to 36, further comprising a cleaning control device to initiate a cleaning cycle, to pass cleaning liquid through one or more of the compressor, dewatering device and comminuter and to discharge spent cleaning fluid through an outlet drain orifice.
38. Apparatus as set out in clause 37, wherein the dewatering device and the compressor comprise screw conveyors drivable in a reverse direction during a cleaning cycle.
39. Apparatus as set out in clause 37 or clause 38, further comprising a sensor to sensing the presence of waste to be treated to enable initiation of a cleaning cycle when presence of waste in the apparatus is no longer detected.
40. Apparatus for processing kitchen waste comprising food waste, the apparatus comprising an inlet for receiving a batch of the waste and comminuting means communicating with the inlet for comminuting the waste to provide a comminuted waste, dewatering means for dewatering the comminuted waste to provide a dewatered waste, compressing means for compressing the dewatered waste to produce a compressed waste, and an outlet for processed waste.
41. Apparatus as set out in clause 40 further comprising delivering means for delivering a drying agent such as a cementitious powder to be mixed with the compressed waste and means for mixing the compressed waste with the delivered drying agent to form waste granules.
Claims (48)
- Claims: Apparatus for processing, at the premises of a kitchen, kitchen waste comprising food waste, the apparatus comprising: an inlet for receiving the kitchen waste; a comminuterto comminute the received waste to provide comminuted waste; a dewatering device to dewater the comminuted waste to provide dewatered comminuted waste; a compressor to compress the dewatered comminuted waste; and an outlet to provide processed waste ready for collection, the apparatus further comprising a hopper to contain a drying agent, a mixer to mix the compressed waste with the drying agent and a feed mechanism for dispensing the drying agent from the hopper for delivery to the mixer.
- 2. Apparatus according to claim 1, wherein the compressor comprises a screw conveyor having a housing containing a screw flight and a core.
- 3. Apparatus according to claim 2, wherein the core increases in diameter from an inlet towards an outlet of the screw conveyor such that a gap between the screw and a housing of the screw decreases towards the outlet.
- 4. Apparatus as claimed in claim 2 or 3, wherein the pitch of the screw conveyor decreases from the inlet towards the outlet.
- 5. Apparatus as claimed in claim 2, 3 or 4, wherein the housing of the compressor screw conveyor is arranged to open to allow cleaning.
- 6. Apparatus according to any preceding claim, wherein the drying agent is a powder.
- 7. Apparatus according to any preceding claim, wherein the drying agent comprises at least one of Portland cement, quicklime, finely divided silica, a hydraulic mortar mix.
- 8. Apparatus according to any of claims 1 to 6, wherein the drying agent comprises a hydraulic mortar mix comprising silica, hydrated lime, and calcium magnesium carbonate.
- 9. Apparatus according to any of claims 1 to 6, wherein the drying agent comprises a hydraulic mortar mix comprising silica, hydrated lime, and calcium magnesium carbonate and a polymer latex such as styrene butadiene latex.
- 10. Apparatus according to any of claims 1 to 6, wherein the drying agent comprises crushed quartz 60%, hydrated lime 30%, SBR latex 5%, and Dolomite 5%, by weight.
- 11. Apparatus according to any of claims 1 to 6, wherein the drying agent comprises a glass block mortar (GBM).
- 12. Apparatus according to any any preceding claim, wherein the drying agent comprises a fungicide.
- 13. Apparatus according to claim 12, wherein the fungicide comprises copper sulphate, another copper salt, or a wood preservative.
- 14. Apparatus according to any preceding claim, wherein the comminuter is arranged to provide particles of about 2mm in size.
- 15. Apparatus according to any preceding claim, wherein the dewatering device is arranged to result in 50-70% of the weight of the waste being lost as liquid water.
- 16. Apparatus according to any preceding claim, wherein the compressor is arranged to apply a pressure of at least 25MPa -35MPa to dewatered the waste.
- 17. Apparatus according to any of the preceding claims, further comprising a source of the waste, wherein the waste comprises one or more of: food preparation scraps such as cuttings and/or peelings; left over food; food left on plates; cooked food; uncooked food.
- 18. Apparatus according to any preceding claim, wherein the inlet has a lid moveable between a closed position and an open position and the inlet communicates with a hopper having an outlet, the hopper outlet communicating with the comminuter by a door mechanism, and wherein the door mechanism and the lid are interlocked such that the door mechanism opens to supply food waste to the comminuter only when the lid is in the closed position and such that the lid is openable to allow a user to add food waste into the hopper only when the door mechanism is closed.
- 19. Apparatus as claimed in any preceding claim, wherein the comminuter comprises at least a pair of contra-rotating driven knife or blade bearing shafts defining a nip through which waste is forced.
- 20. Apparatus as claimed in any preceding claim, wherein the comminuter comprises a receiving chamber to transfer waste to the dewatering device, the receiving chamber having a stirring member for stirring and/or guiding the waste.
- 21. Apparatus as claimed in claim 20, wherein the stirring member is shaped to urge waste into the dewatering device.
- 22. Apparatus as claimed in any preceding claim, wherein the dewatering device comprises an Archimedean screw having a housing with apertures for egress of water.
- 23. Apparatus as claimed in any of claims 1 to 21, wherein the dewatering device and the compressor comprise Archimedean screws having screw flights arranged on cores that are coupled to one to the other or are integral or unitary.
- 24. Apparatus as claimed in any preceding claim, wherein the mixer comprises a mixing chamber containing at least one rotatable blade member.
- 25. Apparatus as claimed in any preceding claim, wherein a valve is provided at an outlet of the compressor, which valve is moveable between an open position and a closed position.
- 26. Apparatus as claimed in any preceding claim, further comprising a cleaning control device to initiate a cleaning cycle, to pass cleaning liquid through one or more of the compressor, dewatering device and comminuter and to discharge spent cleaning fluid through an outlet drain orifice.
- 27. Apparatus as claimed in claim 26, wherein the dewatering device and the compressor comprise screw conveyors drivable in a reverse direction during a cleaning cycle.
- 28. Apparatus as claimed in claim 26 or claim 27, further comprising a sensor to sensing the presence of waste to be treated to enable initiation of a cleaning cycle when presence of waste in the apparatus is no longer detected.
- 29. Apparatus according to any preceding claim, further comprising bagging means to store the processed waste.
- 30. Apparatus according to claim 29, further comprising heated bag retaining means.
- 31. An apparatus for processing kitchen waste comprising food waste at the premises of the kitchen, substantially as hereinbefore described with reference to and/or as illustrated in the accompanying drawings.
- 32. A method of producing processed food waste from kitchen waste comprising food waste, which method comprises: receiving the kitchen waste; comminuting the received waste to provide comminuted waste; dewatering the comminuted waste to provide dewatered comminuted waste; compressing the dewatered comminuted waste; mixing the compressed waste with a drying agent; and providing from the outlet processed waste ready for collection.
- 33. A method according to claim 32, wherein the drying agentis a powder.
- 34. A method according to claim 32, wherein the drying agent is a cementitious powder and the mixing forms cementitious waste granules.
- 35. A method according to claim 32, 33 or 34, wherein the drying agent comprises at least one of Portland cement, quick lime, finely divided silica, a hydraulic mortar mix.
- 36. A method according to claim 32, 33 or 34, wherein the drying agent comprises a hydraulic mortar mix comprising silica, hydrated lime, and calcium magnesium carbonate.
- 37. A method according to claim 32, 33 or 34, wherein the drying agent comprises a hydraulic mortar mix comprising silica, hydrated lime, and calcium magnesium carbonate and a polymer latex such as styrene butadiene latex.
- 38. A method according to claim 32, 33 01 34, wherein the drying agent comprises crushed quartz 60%, hydrated lime 30%, SBR latex 5%, and Dolomite 5%, by weight.
- 39. A method according to claim 32, 33 or 34, wherein the drying agent comprises a glass block mortar (GBM).
- 40. A method according to any of claims 32 to 39, wherein the drying agent comprises a fungicide.
- 41. A method according to claim 40, wherein the fungicide comprises copper sulphate, another copper salt, or a wood preservative.
- 42. A method according to any of claims 32 to 41, wherein comminuting the received waste provides particles of about 2mm in size.
- 43. A method according to any of claims 32 to 42, wherein dewatering the comminuted waste results in 50-70% of the weight of the waste being lost as liquid water.
- 44. A method according to any of claims 32 to 43, wherein during compression of the dewatered waste a pressure of at least 25MPa -35MPa is applied to the waste.
- 45. A method according to any of claims 32 to 44, wherein the waste comprises one or more of: food preparation scraps such as cuttings and/or peelings; left over food; food left on plates; cooked food; uncooked food.
- 46. A method of producing processed food waste from kitchen waste comprising food waste, substantially as hereinbefore described with reference to and/or as illustrated in the accompanying drawings.
- 47. A method of disposing of waste, such as food waste, from the kitchens of a plurality of premises, the method comprising: collecting processed waste produced by an apparatus in accordance with any of claims Ito 31 or a method in accordance with any of claims 32 to 46 from the plurality of premises; and disposing of 2 0 the collected processed waste.
- 48. A method according to claim 47, wherein disposing comprises transporting the processed waste to a processing facility and incorporating the processed waste into manufactured products at the processing facility or (b) to transporting the processed waste to a waste disposal location.
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GBGB1018150.1A GB201018150D0 (en) | 2010-10-27 | 2010-10-27 | A method of and apparatus for treating waste and a waste product |
GB1113457.4A GB2485014B (en) | 2010-10-27 | 2011-08-04 | A method of and apparatus for treating waste and a waste product |
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CN112997888A (en) * | 2021-02-23 | 2021-06-22 | 淮阴工学院 | Preparation device and method of bean curd cat litter |
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GB201410696D0 (en) | 2014-07-30 |
GB2512763B (en) | 2015-03-18 |
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