WO2015092387A1 - Améliorations apportées à une technologie de friture - Google Patents

Améliorations apportées à une technologie de friture Download PDF

Info

Publication number
WO2015092387A1
WO2015092387A1 PCT/GB2014/053722 GB2014053722W WO2015092387A1 WO 2015092387 A1 WO2015092387 A1 WO 2015092387A1 GB 2014053722 W GB2014053722 W GB 2014053722W WO 2015092387 A1 WO2015092387 A1 WO 2015092387A1
Authority
WO
WIPO (PCT)
Prior art keywords
oil
food
cooking
cooking oil
frying
Prior art date
Application number
PCT/GB2014/053722
Other languages
English (en)
Inventor
Andrew CLAY
Original Assignee
Oil Preservation Technologies Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Oil Preservation Technologies Ltd filed Critical Oil Preservation Technologies Ltd
Publication of WO2015092387A1 publication Critical patent/WO2015092387A1/fr

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B3/00Refining fats or fatty oils
    • C11B3/10Refining fats or fatty oils by adsorption
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D39/00Filtering material for liquid or gaseous fluids
    • B01D39/08Filter cloth, i.e. woven, knitted or interlaced material
    • B01D39/086Filter cloth, i.e. woven, knitted or interlaced material of inorganic material
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
    • C11B13/00Recovery of fats, fatty oils or fatty acids from waste materials
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2239/00Aspects relating to filtering material for liquid or gaseous fluids
    • B01D2239/10Filtering material manufacturing
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/74Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes

Definitions

  • This invention relates to improvements in technology relating to methods for the in situ treatment of cooking oils and fats.
  • references to oils should be interpreted as being references to animal, vegetable, nut or synthetic oils and fats (which are generally solid at room temperatures).
  • references to fryers herein should be taken as including any frying equipment, chamber, pan, tank, commercial, domestic or industrial fryer.
  • Deep fat frying has become one of the most popular methods of cooking in domestic, restaurant and industrial establishments throughout the World. Because of the high temperatures involved (typically 160 to 200°C) it is relatively quick, cooks food right through to the middle, generates a distinctive crust on the food and perhaps most importantly produces rich and complex flavours and food textures, which are very appealing to the consumer.
  • Cooking oil is expensive: high end olive oils are more expensive per litre than petrol or diesel and the price of even lower end cooking oils is comparable to that of petrol or diesel. Cooking oils have to be replaced frequently as the oils degrade during the cooking process, as more fully explained hereinafter. Also cooking oils (and their breakdown products) are absorbed by the food cooked in them which therefore necessitates the operator of a fryer to regularly keep the oil or fat topped up by the addition of extra cooking oil or fat. Cooking in oil therefore comes at a relatively high price compared to boiling in water or roasting in air. The frequent changing of cooking oil in kitchens, restaurants and food preparation industrial sites is also a labour intensive and laborious task, which is costly and increases equipment down-time. Unfortunately it is not possible to extend the life of cooking oils and fats merely by filtering out the food debris which frequently accumulates within them. During use cooking oils and fats do not remain unaltered but begin to chemically breakdown.
  • Cooking oils and fats are commonly referred to as triglycerides but are in fact
  • triacylglycerols i.e. triesters of glycerol (1, 2, 3 propanetriol, which is commonly referred to as glycerine) and three fatty acids.
  • the fatty acids do not need to be of the same type and frequently are not).
  • Common chain lengths for the fatty acids are 12 to 24 carbon atoms with 16 and 18 being particularly favoured.
  • the breakdown of such triglycerides is complex, dependent on numerous factors and is subject to numerous feedback effects but involves three well-understood basic mechanisms: oxidation, polymerisation and hydrolysis.
  • Oxidation occurs when air comes in contact with frying oil, (see for example Josephson and Lindsey 1987, Journal of Food Sciences, 52, 328 and Fischer and Muller 1991, Potato Research, 34, 159). Oxygen from the air reacts with the two unsaturated carbons at the double-bond via a free radical initiated reaction. The oxidation reaction is promoted by high cooking temperatures (typically 190°C and above), the presence of metals (including in particular copper and iron) and the presentation to the air of a large surface area of the oil as well as exposure to UV light, which promotes free radical formation. Initially hydroperoxides are produced but these are unstable and at frying temperatures they rapidly break down (via e.g.
  • Hydrolysis is caused by the reaction of water (a weak nucleophile) with the ester linkage in the triacylglycerol molecule to produce initially a diaglyceride and a free fatty acid, which then further breakdown to produce various compounds including lactones.
  • water a weak nucleophile
  • free fatty acids are frequently associated with a characteristic rancid or acidic flavour.
  • free fatty acids are one of the main constituents of smoke haze and are both a fire and a health hazard.
  • the smoke point of an oil is the temperature at which it is seen to start smoking under specified test conditions.
  • the flashpoint of an oil is the temperature at which volatile products are produced in sufficient concentration and quantity to allow ignition.
  • the fire point of an oil is the temperature at which the rate of production of volatile products is sufficiently high to support continuous combustion of the gases emerging from the surface of the oil.
  • concentration of surfactants in cooking oil on the properties of the food cooked in such oil is well-known (see e.g. Blumenthal MM A New Look At The Chemistry And Physics Of Deep Fat Frying: Food Technology, 1991, 45:2, 68 -71, 94).
  • chips are cooked in fresh unused cooking oil they are light in colour and do not have the rich complex aromas associated with fried potatoes.
  • the oil, during this "break in” phase has only low levels of surfactants (such as free fatty acids), which means that the oil has a relatively high surface tension which prevents the oil having close contact with the food.
  • oils contain increased amounts of trans-fatty acid side chains on the glycerol backbone, which are a material health hazard.
  • pancreatic enzymes lipases
  • bile secretions The resultant fatty acids and glycerol are then absorbed by cells lining the intestines called enterocytes, where they are re-esterified into triglycerides and transported to the liver as chylomicrons.
  • enterocytes cells lining the intestines
  • the fatty acids are repackaged into triacylglycerols and phosphatidylcholine and thence into lipoproteins.
  • High levels of trans fatty acids in the diet are associated with raised serum levels of low density lipoprotein (LDL) cholesterol and with lower levels of high density lipoprotein (HDL) cholesterol in humans.
  • Raised serum LDL and reduced serum HDL levels are associated with coronary artery disease, increased risk of stroke and elevated blood pressure as they decrease the health of the endothelium, the cells lining the arteries of the body which are essential for good cardiovascular health.
  • Studies in humans further demonstrate that trans fats increase inflammation in the body, a potent risk factor for cardiovascular disease, diabetes, and other diseases. Studies in primates have
  • trans fats cause weight gain, especially increasing abdominal fat, which has the greatest metabolic consequences, and worsens insulin resistance, the precursor to diabetes.
  • the amount of trans-fatty acids absorbed in the diet should be kept at low levels.
  • One way of achieving that is to reduce the amount of cooking oil absorbed by fried food.
  • Various ways have been suggested to prolong the useful life of cooking oils. Some of these involve the step of removing the cooking oil from the fryer, followed by the step of subjecting it to one or more treatment methods to remove the contaminants before finally returning the treated oil back to the fryer. Other methods provide for at least the complete cessation of the cooking process, treatment and then the recommencement of the use of the oil.
  • US-A4112129 discloses a method of filtering the cooking oil through a composition comprising by weight (i) 47 to 59 parts diatomite, (ii) 28 to 36 parts synthetic calcium silicate hydrate and (iii) 12 to 24 parts synthetic magnesium silicate hydrate.
  • US 4681768A discloses a method for the continuous filtration of cooking oil with a filter made from synthetic calcium silicate. The method involves removal of the oil from the fryer, passing it through the filter and then passing it back into the fryer.
  • GB 2006729 discloses a method for filtering used cooking oils to remove free fatty acids, which uses synthetic calcium silicate but does not disclose an in situ solution suitable for unadapted fryers.
  • US 5870945 discloses a filter cartridge for fitting to a fryer, which includes a mesh housing for containing filtering material which is used to treat the cooking oil outside the fryer prior to its return to the fryer.
  • US 4112129 A discloses a method for extending the life of cooking oil by removing free fatty acids which involves treating the oil with a composition of synthetic calcium silicate hydrate and synthetic magnesium silicate hydrate. US 4112129 A states that the method can be used with conventional cooking oil filtration systems but does not disclose an in situ solution suitable for unadapted fryers which do not have a filtration system.
  • EP 0226413A discloses a filter container provided with a removable filter bag but which cannot be used during the cooking operation.
  • US 6210732 discloses a method of extending the life of cooking oil by the use of a blend of finely milled citric acid and calcium silicate powder, which is added to the hot oil, left for a certain length of time and then removed by filtration.
  • the US 6210732 invention cannot be used during the cooking process.
  • WO 91/11914A discloses a still further treatment method for used cooking oils which uses an amorphous silica and alumina composition, which is either added to the hot oil and then filtered out or put in a container which is permeable to the oil but not the treatment composition.
  • the invention disclosed cannot be used during the cooking operation.
  • US 4330564A discloses a method of treating used cooking oil with a composition including a porous carrier, water and a food compatible acid, with the resultant residue being removed by filtration. The invention disclosed cannot be used the cooking operation.
  • US 3947602A discloses a method of treating cooking oil with a food compatible acid and a suitable adsorbent such as activated carbon. The invention disclosed cannot be used during the cooking operation.
  • US 5391385A discloses the treatment of cooking oil with a mixture of 60-80%
  • US 4764384A discloses a method of treating used cooking oil with filtering media comprising synthetic amorphous silica, synthetic amorphous magnesium silicate and diatomaceous earth.
  • US 5354570A discloses a method of frying food in cooking oils with a porous rhyolitic powder which selectively reduces the concentration of certain surfactants, whilst the cooking process is on-going.
  • JP 07-148073A discloses a method of treating cooking oil using finely pulverized zeolite stones which are inserted into a permeable bag which is itself placed into the fryer, with or without food also being present.
  • the above methods either require the addition of powders to the oil, which is undesirable as they may contaminate and change the texture and taste of any food cooked therein or require the a further container to be added to oil, which will often be problematical during use of the fryer.
  • Foaming is encountered with the filters the subject of the BBM Patents particularly in cooking environments where a lot of hydrolysis takes place due to large amounts of wet food being cooked (for example frozen chips).
  • Silasorb (Celite Corporation, Denver, Colo.) which is a synthetic calcium silicate, as their filter medium because it is very effective in lowering free fatty acid concentration. Silasorb lowers the free fatty acid (FFA) concentration of the oil by a combination of adsorption and neutralization. The use of Silasorb, however, often darkens the oil.
  • FFA free fatty acid
  • the product of the neutralization of a fatty acid with an alkaline metal is a fatty acid soap.
  • the amount of soap formed is dependent on the amount of alkaline metal present, and the initial percentage of free fatty acids in the oil. When the soap level is high, the oil foams.
  • Silasorb in order to lower the free fatty acid concentration sometimes results in uncontrollable foaming."
  • concentration of such calcium fatty acid salts in cooking oils, exposed to the filters disclosed in the BBM Patents may be very low in absolute terms (below 3 ppm and possibly even below 1 ppm) it can still give rise to foaming in practice as the polar calcium ions tend to become concentrated at the surface of the oil, from which they are pushed out.
  • a method of preserving cooking oil including by reducing the extent of foaming and/or the build up of free fatty acids in the cooking oil during its use in the frying of food, the method comprising providing in a cooking vessel a body of cooking oil, locating in said body of cooking oil a solid, calcium-containing filtering medium, locating in said body of cooking oil means for reducing the extent of flow of oil over the surface of said filtering medium during the food frying, locating food within said body of oil and heating the cooking oil to effect frying of the food.
  • the invention provides a method of treating cooking oil during frying operations which comprises in situ treatment of the oil with a solid filter treatment material of the type exemplified in the BBM Patents.
  • the flow of oil over the surface of the filtering medium may be modified by at least partially enclosing or encasing the filtering medium to reduce the frequency of occurrence or eradicate foaming.
  • the filtering medium may be in any suitable form, for instance, a single block or loose material in granular form or in the form of beads.
  • the filtering medium is at least partially surrounded by a foraminous barrier. More preferably, the barrier extends laterally adjacent said filtering medium.
  • the barrier forms at least part of a container or enclosure within which the filtering medium is located.
  • the container may be, for instance, of a box-like
  • the container may be an entirely separate item to the cooking vessel.
  • the container may be at least partly integral with the cooking vessel.
  • the filtering medium may contain a minor amount of microsilica.
  • An air entraining agent may be added to the filtering medium during its manufacture so as to create numerous pores in the structure of the medium.
  • the present invention also provides a method of preserving cooking oil, including by reducing the extent of foaming and/or the build up of free fatty acids in the cooking oil during its use in the frying of food, the method comprising providing in a cooking vessel a body of cooking oil, locating in said body of cooking oil a solid, calcium-containing filtering medium and locating food within said body of oil and heating the cooking oil to effect frying of the food, the filter medium containing a minor amount of microsilica.
  • the present invention further provides a method of preserving cooking oil, including by reducing the extent of foaming and/or the build up of free fatty acids in the cooking oil during its use in the frying of food, the method comprising providing in a cooking vessel a body of cooking oil, locating in said body of cooking oil a solid, calcium-containing filtering medium, locating food within said body of oil and heating the cooking oil to effect frying of the food, an air entraining agent being added to the filtering medium during its manufacture so as to create numerous pores in the structure of the medium.
  • the present invention provides a deep oil or fat fryer having a depression or recess for releasably holding, or providing at least a part of, an enclosure for a filtering medium, said enclosure being provided with means for reducing, in use, the extent of flow of oil over the surface of said filtering medium during food frying.
  • the present invention provides a calcium-containing filtering medium for use in preserving cooking oil, the medium containing a minor amount of microsilica.
  • the present invention provides a calcium-containing filtering medium for use in preserving cooking oil, the medium having had added to it during its manufacture an air entraining agent so as to create numerous pores in the structure of the medium.
  • a deep oil or fat fryer having a base or sidewall formed with a depression or recess comprising or for receivably holding or interfacing with an enclosure or cover or comprising (at least in part) such an enclosure or cover so as to reduce the frequency of occurrence or eradicate foaming.
  • the invention still further provides a method for reducing the frequency of occurrence or eradicating the foaming associated with the use of the filter means of the type disclosed in the BBM Patents by the addition of microsilica or similar sized silica particles to the pastes from which such filters are made.
  • the invention yet further provides a method for improving the performance of the filter means of the type disclosed in the BBM Patents by the addition of a suitable air entraining agent to the pastes from which such filter means are made.
  • Fig 1 shows an enclosure with a single piece filter.
  • Fig 2 shows an enclosure with multiple loose filter particles.
  • Fig 3 shows a fryer with a side wall formed for connectably receiving an enclosure of the invention.
  • Fig 4 shows a fryer with a base with a recess for receivably connecting to an enclosure of the invention.
  • Figure shows a filter made according to the WO 2008/015481 and WO 2009/019512 inventions with a build-up of fatty acid salt soap on its surface.
  • the invention is applicable to the in situ treatment of cooking oils or fats for use in all types of fryers having a capacity between 2 to beyond 100 litres. It may be used with the hydraulic cement filter products such as those described in WO 2008/015481 and WO 2009/019512.
  • an enclosure lcomprising a substantially continuous upper wall , in the form of a slidable lid (not shown), a substantially continuous lower wall 3 and further having four side walls 5, at least two of which 7,9 are perforated with holes or are otherwise partial so as to allow diffusion of the cooking oil between the outside of the enclosure and the inside in a direction substantially perpendicular to the upper and lower walls.
  • the lower and upper walls should not be perforated or partial for the invention described herein to work to best effect.
  • the upper sidewall is in the form of a lid which can be securely placed onto, against or round the lower sidewalls.
  • the lid may be hinged or otherwise connectably attached to the lower sidewalls so as to allow relative movement but may also simply detachably securely fit onto the said sidewalls of the said enclosure. It will be readily apparent to the man skilled in the art that the invention herein described is not limited to enclosures which are in a cuboid or rectangular cuboid form: for example numerous polygonal, cylindrical, oval or triangular forms of container will also work satisfactorily as would containers made from side walls with sides of different lengths or shapes.
  • the side walls of the enclosure may (but do not need to be) welded or spot welded or riveted or otherwise connectably joined together.
  • the side walls may be made as separate pieces or in one piece.
  • the side walls can be made out of food grade stainless steel (grade 316) or out of any material which provides an acceptable degree of rigidity,
  • the said enclosure or cover is used to substantially enclose or cover filter media 9 of the type disclosed in the BBM Patents.
  • the filter medium 9 is a block having holes 11 extending therethrough.
  • the upper and lower walls of the enclosure or cover should ideally be parallel to the upper surface of the filter medium 9 and the perforated side walls should be substantially perpendicular to the surface of the filter medium 9.
  • Fig. 2 shows an enclosure 13, similar to enclosure 1 of Fig 1. and showing the lid 15 in slid back to reveal the filter medium 17, in this example being in the form of spherical balls.
  • the invention also extends to include covers which do not substantially encase the filter media but nonetheless significantly reduce the flow of cooking oil over the surface of the said filter media, caused by thermal convection currents.
  • the cover may form a partial enclosure for the filter or it may comprise for example a single plate or more than one plate.
  • the invention extends also to fryers and frying equipment having a base and/or sidewall formed with a depression or recess comprising or for receivably holding or interfacing with an enclosure or cover or comprising (at least in part) such an enclosure or cover. Examples of such equipment are depicted in Figs. 3 and 4.
  • the partial or complete covering or enclosure of the said filters reduces the frequency of foaming or eradicates it completely as it decreases the concentration of calcium ions which leach out of the filter by reducing the rate of flow, due to thermal convection, of cooking oil across the surface of the filter.
  • the cooking oil typically contains between approximately 0.1 to 2 percent free fatty acids, depending upon, inter alia, the type of oil, what has been cooked in it, the frying temperature and the surface area of the oil exposed to air, this in turn reduces the rate at which calcium and in particular calcium hydroxide and calcium silicate hydrate minerals are attacked by the free fatty acids in the cooking oil.
  • the use of such an enclosure or a cover may also decrease the extent to which calcium hydroxide is dissolved in the water which exists in the cooking oil typically as a suspension or emulsion.
  • the solubility of calcium hydroxide in water is generally inversely related to its temperature (i.e. it decreases as the temperature of the water rises) and given that many cooking oils will be at or near room temperature for prolonged periods when not in use then it is likely that the water in the oil does materially dissolve the calcium hydroxide in the filters.
  • Calcium hydroxide is a major component of the filters disclosed in the BBM Patents, being one of the main reaction products of the main cement minerals alite and belite with water. It typically accounts for between twenty to thirty five percent by weight of the filter products disclosed in the BBM Patents.
  • the cover may also simply protect the filter from water dropping down from the basket or other food containment means, when high water content food is added to the oil: for example solidly frozen chips contain a lot of ice which has a relatively high latent heat capacity and therefore the melting of which materially reduces the temperature of the cooking oil possibly allowing, given that the water has a higher density than the cooking oil, some of the emerging water to simply fall downwards on to the filter.
  • Enclosures or covers of the type herein described also prevent food debris from covering the filter or at least reduce the extent to which that happens. Such food debris may accelerate the degradation of the surface of the said filters.
  • a further advantage of using an enclosure or cover of the type described herein is that it makes it practical to use relatively large numbers of smaller separate filter elements. This is advantageous as the use of a plurality of small filter elements materially increases the surface area of the filter media and promotes their efficacy during operation. Addition of Silica fume/microsilica
  • sillica fume or microsilica is a by-product of the production of silicon or ferrosilicon alloys, which is achieved by the reduction of quartz (the mineral) in an electric furnace. Some SiO is lost as a gas, which is then rapidly oxidised by the oxygen in the air to give a very fine white or grey particulate solid.
  • European patent (UK) No. 0,289,240 further discloses another way of making very small glass particles, which are also suitable for use in the invention disclosed herein.
  • Microsilica suitable for the invention herein described can be obtained from either Metalmin & Co (UK) Ltd of Livermore House, High Street, Great Dunmow, CM6 1 AW, Essex, or from Glassflake Limited of Forster Street, Leeds, LS10 1PW, West Yorkshire.
  • High quality silica fume consists of spherical particles of glass typically with a diameter of about 100 run and having a surface area of 15 to 25 m 2 g- J . Glass flakes made using the technology disclosed in European patent (UK) No. 0,289,240 may be made with very tightly controlled dimensions and even higher surface areas and are particularly suitable for the present application.
  • incorporation of silica fume into cement has several effects due to its strong pozzolanic activity. It accelerates the hydration reactions of the clinker phases (particularly alite). The fine microsilica particles fill the spaces between clinker grains thereby producing a denser paste and stronger overall cement.
  • the addition of microsilica further reduces the amount of free calcium hydroxide produced by the hydration of alite and belite and promotes the production of calcium silicate hydrate gel.
  • the use of microsilica has been known to be beneficial for the production of cement in the construction industry the effect of the addition of microsilica in filters of the type disclosed in the BBM Patents to reduce foaming has not hitherto been shown. The effect is further described by reference to example 4 below. Without wishing to be bound by any theory it is thought that the reduction in foaming demonstrated in example 4 is caused by the greater resistance to acid attack of CSH gels relative to calcium hydroxide and their lower solubility in water dissolved in the oil.
  • the entrained air void system in cement can be viewed and determined from the examination of a cut and polished section of a hardened cement sample, using microscopic techniques in accordance with ASTM C457 (standard test method for microscopical determination parameters of the air void system in hardened concrete).
  • Such air voids provide empty spaces within the cement or concrete and are known to act as storage sites for freezing water moving in the capillary pores, thereby relieving the pressure generated during freezing and preventing damage to the cement or concrete.
  • air entraining agents to mixtures of the type used to make the filters of the type described in the BBM Patents produces very much more porous filters, which absorb very considerably much more free fatty acid than filters without such air entraining agents.
  • air entraining agents There are a number of well-known types of air entraining agents.
  • surfactants typically include for example wood derived acid salts, wood rosin, tall oil, vegetable oil acid salts such as the alkanolamine salt of coconut oil, synthetic detergents such as alkyl-aryle sulfonates and sulfates such as dodecylbenzenesulfonate.
  • the surfactant used in the invention disclosed herein must be non-toxic. The man skilled in the art will readily be able to identify numerous such non-toxic air entraining agents suitable for use in the invention herein described.
  • Alborg white clinker is made using an extremely pure limestone originating from a marine deposit which is now located in Denmark.
  • a typical composition of the Alborg clinker used is:- Si0 2 25.0%
  • the clinker has a very low free iron content which is important as iron is a powerful pro-oxidant trace metal, (see for example supra.
  • the mix to make the filters comprised three parts of clinker to one part of OPC. Thorough mixing of the clinker and OPC using an industrial mixer took place and then sufficient water was added to give a good paste.
  • WO/2013/121206 and as further described in that patent application and were then allowed to cure until fully set. Thereafter they were dried in an industrial oven for 72 hours at 130°C to remove excess water and were then sealed in water impermeable wrapping.
  • the dimensions of the filter were approximately 15 cm x 2 cm x 9 cm with 15 holes each with a diameter of approximately 2 cm: (these figures ignore slight tapering of the filter to facilitate extraction from the mould).
  • the filters were subjected to ICP-MS analysis as was an unused filter from the same batch.
  • the unused filter had levels of calcium, aluminium and iron levels of 45%, 2% and 0.2% respectively. These values act as a positive control for the used filters.
  • the frying trials from experiment 1 were repeated but on this occasion the filters were encased in enclosures of the type illustrated in fig 2 made in accordance with the inventions disclosed herein.
  • the location of the filter in example 2 was the same as for example 1 but in this instance only one of the filters showed the waxy brown layer, which was very thin and not continuous. Additionally the amount of calcium depletion in the upper 6 mm layer was considerably less than was seen in example 1: the depletion was only 20% (from 45% with the unused filter to 36% for the used filter).
  • the upper layer was also less friable and the material much more tightly secured into the matrix of the filter as was clearly visible under an electron microscope.
  • Example 1 was repeated but this time the composition of the filter was changed so that microsilica was added to the mix of example 1.
  • the amount of microsilica added was ten percent by weight of the weight of the dry mix of clinker and OPC.
  • the resulting filters were used without enclosures.
  • Example 1 was repeated but this time a small amount of the air entraining agent, microair 119 (manufactured by BASF) was added to the mixture.
  • the amount of microair 119 added was approximately 25 ml to 6 kg of dry mix (OPC and clinker). It was surprisingly found that this had a dramatic effect on the filters thereby produced, which although having a volume of approximately 151 cm 3 (the same as for the filters previously used in these experiments) weighed only 260 gms - about 20 gms lighter than the filters made in example 1.
  • Electron microscopy revealed a network of very small pores in the filters. Such filters exhibited a markedly improved ability to reduce FFA build up. Below are tabulated the average free fatty acid concentrations for the last two trial runs for this set (five days frying per trial):-

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Textile Engineering (AREA)
  • Microbiology (AREA)
  • Edible Oils And Fats (AREA)

Abstract

L'invention concerne un procédé de préservation d'huile de cuisson, comprenant la réduction de l'ampleur du moussage et/ou de l'accumulation d'acides gras libres dans l'huile de cuisson pendant son utilisation pour frire des aliments, comprenant l'introduction dans un récipient de cuisson d'un volume d'huile de cuisson et le placement dans l'huile de cuisson d'un milieu filtrant solide contenant du calcium. L'aliment est placé dans l'huile et l'huile est chauffée pour frire l'aliment. Le milieu filtrant comprend une quantité mineure de microsilice. En outre, ou à la place, un agent entrainant l'air est ajouté au milieu filtrant pendant sa fabrication pour créer de nombreux pores dans la structure du milieu. En outre, ou à la place, un moyen de réduction de l'ampleur du flux de l'huile sur la surface dudit milieu filtrant est placé dans l'huile pendant la friture de l'aliment.
PCT/GB2014/053722 2013-12-16 2014-12-16 Améliorations apportées à une technologie de friture WO2015092387A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB1322146.0 2013-12-16
GBGB1322146.0A GB201322146D0 (en) 2013-12-16 2013-12-16 Improvements in frying technology

Publications (1)

Publication Number Publication Date
WO2015092387A1 true WO2015092387A1 (fr) 2015-06-25

Family

ID=50030943

Family Applications (2)

Application Number Title Priority Date Filing Date
PCT/GB2014/053722 WO2015092387A1 (fr) 2013-12-16 2014-12-16 Améliorations apportées à une technologie de friture
PCT/GB2014/053723 WO2015092388A2 (fr) 2013-12-16 2014-12-16 Améliorations apportées au processus de friture

Family Applications After (1)

Application Number Title Priority Date Filing Date
PCT/GB2014/053723 WO2015092388A2 (fr) 2013-12-16 2014-12-16 Améliorations apportées au processus de friture

Country Status (2)

Country Link
GB (1) GB201322146D0 (fr)
WO (2) WO2015092387A1 (fr)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019171251A1 (fr) 2018-03-05 2019-09-12 Fripura Limited Perfectionnements apportés à une technologie de friture

Citations (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US112129A (en) 1871-02-28 Improvement in preserving fish by freezing
US3947602A (en) 1974-04-29 1976-03-30 Bernard Friedman Treatment of cooking oil
US4112129A (en) 1977-09-14 1978-09-05 Johns-Manville Corporation Cooking oil treating system and composition therefor
GB2006729A (en) 1977-09-14 1979-05-10 Johns Manville Fast flow rate coarse synthetic hydrous calcium silicate.
US4330564A (en) 1979-08-23 1982-05-18 Bernard Friedman Fryer oil treatment composition and method
EP0226413A2 (fr) 1985-12-06 1987-06-24 Oil Process Systems, Inc. Dispositif de filtrage
US4681768A (en) 1985-08-14 1987-07-21 Reagent Chemical & Research Company Treatment of cooking oils and fats
US4764384A (en) 1986-04-03 1988-08-16 Gycor International Ltd. Method of filtering spent cooking oil
EP0289240A1 (fr) 1987-04-23 1988-11-02 Glassflake Ltd Procédé et appareil de fabrication de paillettes en verre
US4988440A (en) * 1989-01-30 1991-01-29 Filtercorp, Inc. Cooking oil filter
WO1991011914A1 (fr) 1990-02-15 1991-08-22 Pq Corporation Procede de traitement de l'huile de friture utilisant une composition d'alumine et de silice amorphe
US5354570A (en) 1987-09-21 1994-10-11 Oil Process Systems, Inc. Extended use of filter aid in oil
JPH07148073A (ja) 1993-12-01 1995-06-13 Yoshihide Shibano ゼオライトを用いた調理用器材
US5597600A (en) 1995-06-05 1997-01-28 The Dallas Group Of America, Inc. Treatment of cooking oils and fats with magnesium silicate and alkali materials
US5870945A (en) 1997-01-17 1999-02-16 Bivens; Thomas H. Portable filtration and treatment apparatus
US6187355B1 (en) * 1998-06-08 2001-02-13 The University Of Georgia Research Foundation, Inc. Recovery of used frying oils
US6210732B1 (en) 2000-02-03 2001-04-03 James A. Papanton Cooking oil additive and method of using
US20070154603A1 (en) * 2005-12-30 2007-07-05 Withiam Michael C Treatment of cooking oils and fats with sodium magnesium aluminosilicate materials
WO2008015481A2 (fr) 2006-08-03 2008-02-07 Bbm Technology Ltd Préservation de liquides organiques
WO2009019512A1 (fr) 2007-08-03 2009-02-12 Bbm Technology Ltd Conservation de liquides organiques
WO2013121206A2 (fr) 2012-02-14 2013-08-22 Bbm Technology Ltd. Procédé et appareil de moulage

Patent Citations (22)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US112129A (en) 1871-02-28 Improvement in preserving fish by freezing
US3947602A (en) 1974-04-29 1976-03-30 Bernard Friedman Treatment of cooking oil
US4112129A (en) 1977-09-14 1978-09-05 Johns-Manville Corporation Cooking oil treating system and composition therefor
GB2006729A (en) 1977-09-14 1979-05-10 Johns Manville Fast flow rate coarse synthetic hydrous calcium silicate.
US4330564A (en) 1979-08-23 1982-05-18 Bernard Friedman Fryer oil treatment composition and method
US4681768A (en) 1985-08-14 1987-07-21 Reagent Chemical & Research Company Treatment of cooking oils and fats
EP0226413A2 (fr) 1985-12-06 1987-06-24 Oil Process Systems, Inc. Dispositif de filtrage
US4764384A (en) 1986-04-03 1988-08-16 Gycor International Ltd. Method of filtering spent cooking oil
EP0289240A1 (fr) 1987-04-23 1988-11-02 Glassflake Ltd Procédé et appareil de fabrication de paillettes en verre
US5354570A (en) 1987-09-21 1994-10-11 Oil Process Systems, Inc. Extended use of filter aid in oil
US4988440A (en) * 1989-01-30 1991-01-29 Filtercorp, Inc. Cooking oil filter
WO1991011914A1 (fr) 1990-02-15 1991-08-22 Pq Corporation Procede de traitement de l'huile de friture utilisant une composition d'alumine et de silice amorphe
US5391385A (en) 1990-02-15 1995-02-21 The Pq Corporation Method of frying oil treatment using an alumina and amorphous silica composition
JPH07148073A (ja) 1993-12-01 1995-06-13 Yoshihide Shibano ゼオライトを用いた調理用器材
US5597600A (en) 1995-06-05 1997-01-28 The Dallas Group Of America, Inc. Treatment of cooking oils and fats with magnesium silicate and alkali materials
US5870945A (en) 1997-01-17 1999-02-16 Bivens; Thomas H. Portable filtration and treatment apparatus
US6187355B1 (en) * 1998-06-08 2001-02-13 The University Of Georgia Research Foundation, Inc. Recovery of used frying oils
US6210732B1 (en) 2000-02-03 2001-04-03 James A. Papanton Cooking oil additive and method of using
US20070154603A1 (en) * 2005-12-30 2007-07-05 Withiam Michael C Treatment of cooking oils and fats with sodium magnesium aluminosilicate materials
WO2008015481A2 (fr) 2006-08-03 2008-02-07 Bbm Technology Ltd Préservation de liquides organiques
WO2009019512A1 (fr) 2007-08-03 2009-02-12 Bbm Technology Ltd Conservation de liquides organiques
WO2013121206A2 (fr) 2012-02-14 2013-08-22 Bbm Technology Ltd. Procédé et appareil de moulage

Non-Patent Citations (8)

* Cited by examiner, † Cited by third party
Title
"Standard Methods for Oils, Fats and Derivatives", 1979, PERGAMON PRESS
BELITZ; GROSCH: "Food Chemistry", 1999, SPRINGER-VERLAG, pages: 211
BLUMENTHAL MM, A NEW LOOK AT THE CHEMISTRY AND PHYSICS OF DEEP FAT FRYING: FOOD TECHNOLOGY, vol. 45, 1991, pages 2,68 - 71,94
FISCHER; MULLER, POTATO RESEARCH, vol. 34, 1991, pages 159
JOSEPHSON; LINDSEY, JOURNAL OF FOOD SCIENCES, vol. 52, 1987, pages 328
SONNTAG: "Bailey's industrial Oil and fat Products", vol. 1, 1979, JOHN WILEY AND SONS, pages: 152
WARNER ET AL., JOURNAL OF FOOD SCIENCE, vol. 39, 1974, pages 761
WEISS: "Food Oils and Their Uses, Wesport", 1983, THE AVI PUBLISHING CO.

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2019171251A1 (fr) 2018-03-05 2019-09-12 Fripura Limited Perfectionnements apportés à une technologie de friture

Also Published As

Publication number Publication date
WO2015092388A2 (fr) 2015-06-25
GB201322146D0 (en) 2014-01-29

Similar Documents

Publication Publication Date Title
JP5508010B2 (ja) 有機液体の保存法
EP2187755B1 (fr) Corps en ciment pour la conservation d'huile de cuisson
EP2449070B1 (fr) Procede d'elimination de composants du propanol non souhaites a partir d'une huile de triglycerides non utilisee
US20080102181A1 (en) Rejuvenation of used cooking oil
US5200224A (en) Method of treating fryer cooking oil
EP3761838B1 (fr) Perfectionnements apportés à une technologie de friture
WO2015092387A1 (fr) Améliorations apportées à une technologie de friture
US9636657B2 (en) Hydraulically set cement body for preservation of organic liquids
WO2016034897A1 (fr) Améliorations apportées à une technologie de friture
US10238126B2 (en) Frying technology
US10342240B2 (en) Frying technology
US20150328562A1 (en) Method and Structure for Adsorbing Contaminants from Liquid
US20200170274A1 (en) Hydraulically set cement body for preservation of organic liquids
EP0309235A2 (fr) Utilisation prolongée d'un agent filtrant dans l'huile

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 14825179

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 14825179

Country of ref document: EP

Kind code of ref document: A1