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SE463315B - PROCEDURE FOR EXTRACTION OF OIL FROM FISHING - Google Patents

PROCEDURE FOR EXTRACTION OF OIL FROM FISHING

Info

Publication number
SE463315B
SE463315B SE8900206A SE8900206A SE463315B SE 463315 B SE463315 B SE 463315B SE 8900206 A SE8900206 A SE 8900206A SE 8900206 A SE8900206 A SE 8900206A SE 463315 B SE463315 B SE 463315B
Authority
SE
Sweden
Prior art keywords
temperature
heating
fish
frozen
oil
Prior art date
Application number
SE8900206A
Other languages
Swedish (sv)
Other versions
SE8900206L (en
SE8900206D0 (en
Inventor
Felix Eriksson
Original Assignee
Felix Eriksson
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 Felix Eriksson filed Critical Felix Eriksson
Priority to SE8900206A priority Critical patent/SE463315B/en
Publication of SE8900206D0 publication Critical patent/SE8900206D0/en
Priority to AU49543/90A priority patent/AU4954390A/en
Priority to EP90902407A priority patent/EP0454755A1/en
Priority to PCT/SE1990/000012 priority patent/WO1990008179A1/en
Publication of SE8900206L publication Critical patent/SE8900206L/en
Publication of SE463315B publication Critical patent/SE463315B/en
Priority to NO91912833A priority patent/NO912833L/en
Priority to FI913499A priority patent/FI913499A0/en

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
    • C11B1/00Production of fats or fatty oils from raw materials
    • C11B1/12Production of fats or fatty oils from raw materials by melting out
    • 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
    • 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

Landscapes

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

Description

15 20 25 30 35 463 E? Un 2 2-4 dygn. Efter denna djupfrysningsperiod tas materia- let ut och förvaras i en omgivning med en temperatur inom området mellan +5°C och 20°C i och för tinande, varefter detsamma uppvärms till över +30°C och före- trädesvis till en temperatur inom omrâdet mellan +40°C och +50°C samt hålles vid denna temperatur under en tid av minst l timme. Denna uppvärmning kan företrädes- vis drivas med en sådan hastighet att temperaturen ökar med ca 5-30°C/timme. Under denna uppvärmning förvaras fiskrenset lämpligen i en första, vätskegenom- släppande behållare, t ex en nätkasse med finmaskigt nät eller ett kärl med silduk, som i sin tur lokaliseras i eller över en andra, icke-vätskegenomsläppande behål- lare. Under dylik uppvärmning kommer, såsom utförda försök visat, en §§§EÅQ9ÉPÉ}lêRd$_Yäɧk§ri form av olja att successivt extraheras ur det uppvärmda materia- let och får droppa ur den första, vätskegenomsläppande behållaren ned i den andra, vätskeuppsamlande behållaren. 15 20 25 30 35 463 E? Un 2 2-4 days. After this freezing period, the material is taken out and stored in an environment with a temperature in the range between + 5 ° C and 20 ° C for thawing, after which it is heated to over + 30 ° C and preferably to a temperature within the range between + 40 ° C and + 50 ° C and maintained at this temperature for a period of at least 1 hour. This heating can preferably be operated at such a speed that the temperature increases by about 5-30 ° C / hour. During this heating, the fish cleaner is suitably stored in a first, liquid-permeable container, for example a net bag with a fine-mesh net or a vessel with a screen cloth, which in turn is located in or over a second, non-liquid-permeable container. During such heating, as experiments have shown, a §§§EÅQ9ÉPÉ} læRd $ _Yäɧk§ri form of oil will be gradually extracted from the heated material and allowed to drip from the first, liquid-permeable container into the second, liquid-collecting the container.

Vid de försök som utförts har kunnat konstateras att andelen olja eller oljeformig vätska som erhålls genom processen kan uppgå ända till 70 - 80% räknat på fisk- rensets vikt i_fast form. Den genom processen erhållna oljan är lättflytande vid rumstemperatur (har ungefär samma viskositet som symaskinsolja) och stabil vid förvaring i rumstemperatur på så sätt att dess egen- skaper ej förändras. Därest utgångsmaterialet, dvs fiskrenset, befrias från blodinnehàllande beståndsdelar, såsom hjärta och lever, blir den erhållna oljan klar och ljust gulfärgad, varvid med ökande mängd blodhaltiga beståndsdelar i renset dock erhålls oljor med till- tagande rödfärgning.In the experiments that have been carried out, it has been established that the proportion of oil or oily liquid obtained through the process can amount to as much as 70 - 80% calculated on the weight of the fish cleaner in solid form. The oil obtained by the process is easily liquid at room temperature (has approximately the same viscosity as sewing machine oil) and stable when stored at room temperature in such a way that its properties do not change. To the extent that the starting material, ie the fish cleanser, is freed from blood-containing constituents, such as heart and liver, the resulting oil becomes clear and light yellow, whereby with increasing amounts of blood-containing constituents in the purifier, oils with increasing red color are obtained.

Den erhållna oljan innehåller många värdefulla beståndsdelar, såsom omättade fettsyror, varför den- samma kan användas inom en rad tekniska områden, t ex såsom råmaterial för tillverkning av livs- och läkemedel, kosmetika, smörjmedel, bränslen, etc.The oil obtained contains many valuable constituents, such as unsaturated fatty acids, so that it can be used in a number of technical fields, for example as raw materials for the manufacture of food and pharmaceuticals, cosmetics, lubricants, fuels, etc.

Claims (7)

10 15 20 25 30 Jfl Cm 04 g\ Un PATENTKRAV10 15 20 25 30 J fl Cm 04 g \ Un PATENTKRAV 1. Förfarande för extraktion av olja ur fiskrens, innefattande steget att uppvärma renset till en tempe- ratur över +30°C under förvaring av detsamma i en vätskegenomsläppande behållare från vilken genom upp- värmning extraherad olja ur renset avskiljs genom att droppa ned ur behållaren med återstoden av renset kvarblivande i behållaren, k ä n n e t e c k n a t därav, att fiskrenset i ett inledande steg före upp- värmningen till sagda temperatur djupfryses, dvs fryses till en temperatur under -18°C, varefter detsamma tinas upp ur det djupfrysta tillståndet.A process for extracting oil from a fish cleaner, comprising the step of heating the cleaner to a temperature above + 30 ° C while storing the same in a liquid-permeable container from which oil extracted by heating is separated by dripping out of the container. with the remainder of the purge remaining in the container, characterized in that the fish purifier in an initial step before heating to said temperature is deep-frozen, ie frozen to a temperature below -18 ° C, after which it is thawed out of the deep-frozen state. 2. Förfarande enligt krav l, k ä n n e t e c k - n a t därav, att djupfrysningen drivs till en tempe- ratur inom området mellan -20°C och -30°C.Process according to Claim 1, characterized in that the deep-freezing is operated at a temperature in the range between -20 ° C and -30 ° C. 3. Förfarande enligt krav 1 eller 2, k ä n n e - t e c k n a t därav, att fiskrenset hålles fryst under en tid av åtminstone ett dygn.3. A method according to claim 1 or 2, characterized in that the fish cleaner is kept frozen for a period of at least one day. 4. Förfarande enligt något av föregående krav, k ä n n e t e c k n a t därav, att materialet hålls uppvärmt till en temperatur över +30°C under en tid av minst en timme.4. A method according to any one of the preceding claims, characterized in that the material is kept heated to a temperature above + 30 ° C for a period of at least one hour. 5. Förfarande enligt något av föregående krav, k ä n n e t e c k n a t därav, att sagda uppvärmning genomförs till en temperatur inom området mellan +40°C och +50°C.Process according to any one of the preceding claims, characterized in that said heating is carried out to a temperature in the range between + 40 ° C and + 50 ° C. 6. Förfarande enligt krav 5, k ä n n e t e c k- n a t därav, att temperaturen under sagda uppvärm- ningssteg ökas med en hastighet av 5-30°C per timme.6. A method according to claim 5, characterized in that the temperature is increased during said heating step at a rate of 5-30 ° C per hour. 7. Förfarande enligt något av föregående krav, k ä n n e t e c k n a t därav, att såsom fiskrens används inälvor från laxfisk.7. A method according to any one of the preceding claims, characterized in that entrails from salmonids are used as fish cleaners.
SE8900206A 1989-01-20 1989-01-20 PROCEDURE FOR EXTRACTION OF OIL FROM FISHING SE463315B (en)

Priority Applications (6)

Application Number Priority Date Filing Date Title
SE8900206A SE463315B (en) 1989-01-20 1989-01-20 PROCEDURE FOR EXTRACTION OF OIL FROM FISHING
AU49543/90A AU4954390A (en) 1989-01-20 1990-01-05 Method for extracting oil from fish offal
EP90902407A EP0454755A1 (en) 1989-01-20 1990-01-05 Method for extracting oil from fish offal
PCT/SE1990/000012 WO1990008179A1 (en) 1989-01-20 1990-01-05 Method for extracting oil from fish offal
NO91912833A NO912833L (en) 1989-01-20 1991-07-19 PROCEDURE FOR THE RECOVERY OF OIL FROM FISH WASTE.
FI913499A FI913499A0 (en) 1989-01-20 1991-07-19 FOERFARANDE FOER EXTRAKTION AV OLJA UR FISKRENS.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SE8900206A SE463315B (en) 1989-01-20 1989-01-20 PROCEDURE FOR EXTRACTION OF OIL FROM FISHING

Publications (3)

Publication Number Publication Date
SE8900206D0 SE8900206D0 (en) 1989-01-20
SE8900206L SE8900206L (en) 1990-07-21
SE463315B true SE463315B (en) 1990-11-05

Family

ID=20374812

Family Applications (1)

Application Number Title Priority Date Filing Date
SE8900206A SE463315B (en) 1989-01-20 1989-01-20 PROCEDURE FOR EXTRACTION OF OIL FROM FISHING

Country Status (5)

Country Link
EP (1) EP0454755A1 (en)
AU (1) AU4954390A (en)
FI (1) FI913499A0 (en)
SE (1) SE463315B (en)
WO (1) WO1990008179A1 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004002663A (en) * 2002-03-29 2004-01-08 Shizuoka Prefecture Method for extracting lipid composition containing phospholipid with polyunsaturated fatty acid as constituent from fish internal organ
SE526074C2 (en) * 2003-03-28 2005-06-28 Felix Eriksson Method and apparatus for separating a liquid from a feedstock comprising oily animals such as fish purification
CN109609257A (en) * 2018-12-29 2019-04-12 安徽富煌三珍食品集团有限公司 The extracting method of Yi Zhong Channel-catfish fish guts oil

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2614110A (en) * 1947-06-06 1952-10-14 Sharples Corp Recovery of oil and meal from oil-bearing marine life
US2516071A (en) * 1949-05-06 1950-07-18 Pavia Process Inc Rendering fats

Also Published As

Publication number Publication date
WO1990008179A1 (en) 1990-07-26
AU4954390A (en) 1990-08-13
SE8900206L (en) 1990-07-21
EP0454755A1 (en) 1991-11-06
SE8900206D0 (en) 1989-01-20
FI913499A0 (en) 1991-07-19

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