JPH02219581A - Modified fats and oils for margarine or shortening - Google Patents
Modified fats and oils for margarine or shorteningInfo
- Publication number
- JPH02219581A JPH02219581A JP1040673A JP4067389A JPH02219581A JP H02219581 A JPH02219581 A JP H02219581A JP 1040673 A JP1040673 A JP 1040673A JP 4067389 A JP4067389 A JP 4067389A JP H02219581 A JPH02219581 A JP H02219581A
- Authority
- JP
- Japan
- Prior art keywords
- oils
- fats
- lipase
- oil
- shortening
- 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.)
- Pending
Links
- 239000003921 oil Substances 0.000 title claims abstract description 17
- 239000003925 fat Substances 0.000 title claims abstract description 16
- 235000019197 fats Nutrition 0.000 title claims abstract description 16
- 238000004904 shortening Methods 0.000 title claims abstract description 15
- 235000013310 margarine Nutrition 0.000 title claims abstract description 14
- 239000003264 margarine Substances 0.000 title claims description 13
- 235000019482 Palm oil Nutrition 0.000 claims abstract description 18
- 239000002540 palm oil Substances 0.000 claims abstract description 18
- 235000019198 oils Nutrition 0.000 claims abstract description 16
- 102000004882 Lipase Human genes 0.000 claims abstract description 14
- 108090001060 Lipase Proteins 0.000 claims abstract description 14
- 239000004367 Lipase Substances 0.000 claims abstract description 11
- 235000019421 lipase Nutrition 0.000 claims abstract description 11
- 150000003626 triacylglycerols Chemical class 0.000 claims abstract description 4
- 239000007787 solid Substances 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 abstract description 6
- 239000008157 edible vegetable oil Substances 0.000 abstract description 3
- 238000002844 melting Methods 0.000 abstract description 3
- 230000008018 melting Effects 0.000 abstract description 3
- 239000000203 mixture Substances 0.000 abstract description 3
- 241000228212 Aspergillus Species 0.000 abstract description 2
- 241000222120 Candida <Saccharomycetales> Species 0.000 abstract description 2
- 241000235395 Mucor Species 0.000 abstract description 2
- 235000012424 soybean oil Nutrition 0.000 abstract description 2
- 239000003549 soybean oil Substances 0.000 abstract description 2
- 125000004185 ester group Chemical group 0.000 abstract 2
- 241000894006 Bacteria Species 0.000 abstract 1
- 241000228143 Penicillium Species 0.000 abstract 1
- 241000589516 Pseudomonas Species 0.000 abstract 1
- 241000235527 Rhizopus Species 0.000 abstract 1
- 229920006395 saturated elastomer Polymers 0.000 abstract 1
- 235000002316 solid fats Nutrition 0.000 abstract 1
- 239000000047 product Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 7
- 239000013078 crystal Substances 0.000 description 6
- 235000014593 oils and fats Nutrition 0.000 description 6
- 238000005809 transesterification reaction Methods 0.000 description 5
- 239000007795 chemical reaction product Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 3
- 230000000704 physical effect Effects 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000007670 refining Methods 0.000 description 2
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- LDVVTQMJQSCDMK-UHFFFAOYSA-N 1,3-dihydroxypropan-2-yl formate Chemical compound OCC(CO)OC=O LDVVTQMJQSCDMK-UHFFFAOYSA-N 0.000 description 1
- IIZPXYDJLKNOIY-JXPKJXOSSA-N 1-palmitoyl-2-arachidonoyl-sn-glycero-3-phosphocholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCC\C=C/C\C=C/C\C=C/C\C=C/CCCCC IIZPXYDJLKNOIY-JXPKJXOSSA-N 0.000 description 1
- 240000002791 Brassica napus Species 0.000 description 1
- 235000004977 Brassica sinapistrum Nutrition 0.000 description 1
- 244000020518 Carthamus tinctorius Species 0.000 description 1
- 235000003255 Carthamus tinctorius Nutrition 0.000 description 1
- 244000068988 Glycine max Species 0.000 description 1
- 235000010469 Glycine max Nutrition 0.000 description 1
- 235000019484 Rapeseed oil Nutrition 0.000 description 1
- 240000008042 Zea mays Species 0.000 description 1
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 1
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- OENHQHLEOONYIE-UKMVMLAPSA-N all-trans beta-carotene Natural products CC=1CCCC(C)(C)C=1/C=C/C(/C)=C/C=C/C(/C)=C/C=C/C=C(C)C=CC=C(C)C=CC1=C(C)CCCC1(C)C OENHQHLEOONYIE-UKMVMLAPSA-N 0.000 description 1
- TUPZEYHYWIEDIH-WAIFQNFQSA-N beta-carotene Natural products CC(=C/C=C/C=C(C)/C=C/C=C(C)/C=C/C1=C(C)CCCC1(C)C)C=CC=C(/C)C=CC2=CCCCC2(C)C TUPZEYHYWIEDIH-WAIFQNFQSA-N 0.000 description 1
- 235000013734 beta-carotene Nutrition 0.000 description 1
- 239000011648 beta-carotene Substances 0.000 description 1
- 229960002747 betacarotene Drugs 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 235000005822 corn Nutrition 0.000 description 1
- 239000002285 corn oil Substances 0.000 description 1
- 235000005687 corn oil Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004945 emulsification Methods 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001640 fractional crystallisation Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229940067606 lecithin Drugs 0.000 description 1
- 235000010445 lecithin Nutrition 0.000 description 1
- 239000000787 lecithin Substances 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000008476 powdered milk Nutrition 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 1
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 1
- OENHQHLEOONYIE-JLTXGRSLSA-N β-Carotene Chemical compound CC=1CCCC(C)(C)C=1\C=C\C(\C)=C\C=C\C(\C)=C\C=C\C=C(/C)\C=C\C=C(/C)\C=C\C1=C(C)CCCC1(C)C OENHQHLEOONYIE-JLTXGRSLSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、改質された食用油脂に関するものである。[Detailed description of the invention] [Industrial application field] The present invention relates to modified edible fats and oils.
パーム油を利用した加工油脂で特にマーガリン、ショー
トニングなどにおいては、製品貯蔵中にザラツキの発現
が認められることがある。Processed fats and oils using palm oil, especially margarine and shortening, may develop roughness during product storage.
この現象は、グレイニングや粗大結晶と呼ばれ、特に製
品の外観、機能を著しく低下させたり、ザラツキによる
食感の悪さなどを引き起こし極めて不都合な問題とされ
ている。This phenomenon is called graining or coarse crystals, and is considered to be an extremely inconvenient problem, particularly as it significantly deteriorates the appearance and functionality of the product, and causes roughness and poor texture.
このザラツキ原因成分としては、パーム油中に多く含ま
れる対称TGが影響していることが確認されている。す
なわちこれらのTG酸成分、保存中に油脂の結晶転移に
より、最安定多形であるβ型結晶へ移行し結晶成長を繰
り返すことによりザラツキを起こすものとみられる。It has been confirmed that the component responsible for this roughness is symmetrical TG, which is contained in large amounts in palm oil. In other words, these TG acid components appear to shift to β-type crystals, which are the most stable polymorphs, during storage due to crystal transition of fats and oils, and repeat crystal growth, thereby causing roughness.
これらの点から、実際のソフトタイプのマーガリン等の
製品にはパーム油を20%を越えない範囲で使用されて
いるのが現状であり、これは、パーム油の利用拡大とい
った点からすると非常に大きな問題となっている。From these points of view, the current situation is that palm oil is used in products such as soft margarine within a range that does not exceed 20%, which is extremely important from the perspective of expanding the use of palm oil. This has become a big problem.
この解決策としては、パーム油自体のTG槽構造改質す
る方法、すなわちパーム油中に多く含まれる対称TGを
低減させる方法が考えられているが、これは、特許55
−110195にあるよなTG槽構造ランダム化する方
法、分別結晶化による方法、これらの方法の組合せ法が
有効とされている。As a solution to this problem, a method of modifying the TG tank structure of the palm oil itself, that is, a method of reducing the symmetrical TG that is contained in a large amount in palm oil, is considered.
-110195, a method of randomizing the TG tank structure, a method of fractional crystallization, and a combination of these methods are considered effective.
しかしながら、実際にこれらの方法をソフトタイプのマ
ーガリン、ショートニングに適用した場合、保存中のザ
ラツキの発生は抑えられるものの製品の性状(延展性、
コンシスタンシーなど)や口溶けなどの面でパーム油を
多く利用することが技術的に難しいという間離があった
。However, when these methods are actually applied to soft margarine and shortening, although the occurrence of roughness during storage can be suppressed, the properties of the product (spreadability,
There was a rift in that it was technically difficult to use a large amount of palm oil in terms of consistency, etc.) and melting in the mouth.
(本発明が解決しようとするaU:+
今後高い生産性を持つ油脂資源として注目を浴びている
パーム油を多く利用出来、しかも製品保存中でのザラツ
キの問題がなく、物性的にも非常に良好なソフトタイプ
のマーガリン、ショートニング用改質油脂を開発するこ
とにある。(aU to be solved by the present invention: + It is possible to use a large amount of palm oil, which is attracting attention as an oil resource with high productivity in the future, and there is no problem of roughness during product storage, and it has excellent physical properties. Our objective is to develop modified oils and fats for use in soft margarine and shortening.
(!111題を解決するための手段〕
本発明はパーム油と他の食用油脂とをエステル交換し結
晶粗大の原因となる対称型、2飽和モノオレイックトリ
グリセライド(対称TG)を低減化することによりパー
ム油を高配合利用可能であることを見いだし、しかも物
性的にも非常に優れたソフトタイプのマーガリン、ショ
ートニング川の改質油脂に使用し得ることを見いだし、
本発明を完成させた。(Means for Solving Problem !111) The present invention transesterifies palm oil with other edible fats and oils to reduce symmetrical, disaturated monooleic triglycerides (symmetrical TG) that cause coarse crystals. It was discovered that palm oil could be used in high proportions, and it was also found that it could be used in a soft type margarine and modified shortening oil with excellent physical properties.
The present invention has been completed.
すなわち、本発明は、パーム油とある種の食用油脂とを
リパーゼ存在下でエステル交換することにより、対称型
、2飽和モノオレイックトリグリセライド含量を10%
以下とし、かつエステル交換生成物の33.3°C以上
での固体脂含量(SFC)が2%以下となるソフトタイ
プのマーガリン、ショートニング用改質油脂に関するも
のである。That is, the present invention reduces the content of symmetrical, disaturated monooleic triglycerides to 10% by transesterifying palm oil and certain edible fats and oils in the presence of lipase.
The present invention relates to modified oils and fats for use in soft margarine and shortening, in which the solid fat content (SFC) of the transesterified product at 33.3° C. or higher is 2% or less.
本発明で用いる食用油脂については、植物性油脂、動物
性油脂とそれらの微水fニ脂、分別油なども含まれるが
、エステル交換後の固体脂含量を低く抑えるという点か
ら不飽和脂肪酸含量の多い大豆、菜種、サフラワー サ
ンフラブー コー、ンといった植物性油脂の使用が好ま
しい、また、これらの食用油脂は、単独、あるいは2F
1以上を組み合わせて用いることもできる。The edible fats and oils used in the present invention include vegetable oils, animal fats, and their slight aqueous fats, fractionated oils, etc., but from the viewpoint of keeping the solid fat content low after transesterification, the unsaturated fatty acid content is It is preferable to use vegetable oils such as soybeans, rapeseed, safflower, corn, etc., which have a large amount of edible oil.
A combination of one or more can also be used.
リパーゼとしては、例えば、リゾツブス属(Rhizo
pus)、アスペルギルス属(Aspergillus
)、ペニシリウム属(Penlcillium)、キャ
ンディダ属(Candida)、シュウトモナス属(P
seudosonu+s )、ムコール属(Mucor
)及びジョートリカムll4(Ge。As a lipase, for example, Rhizotubus (Rhizotubus)
pus), Aspergillus spp.
), Penlcilium, Candida, Shutomonas (P
seudosonu+s), Mucor spp.
) and Jotrichum ll4 (Ge.
Lrichum)由来のリパーゼで1.3特異性を有す
るリパーゼを使用する必要がある。1.3特異性のない
リパーゼを使用した場合、T G fill造は、ケミ
カルエステル交換と同様にランダム化が起こり、確かに
対称TGの低減化はおこるが、反応後の生成物中に3飽
和型TG等の高融点TGも同時に生成するために、固体
脂含量が増加する。この傾向は、パーム油含量がアップ
するに従って大きくなるため、これらのリパーゼを使用
して、今回の目的に合致する改質油脂を得ることは困難
となる。It is necessary to use a lipase derived from A.Lrichum) with a specificity of 1.3. 1.3 If a lipase without specificity is used, randomization will occur in TG fill formation similar to chemical transesterification, and although a reduction in symmetric TG will certainly occur, there will be 3-saturation in the product after the reaction. Since high melting point TG such as type TG is also produced at the same time, the solid fat content increases. This tendency increases as the palm oil content increases, making it difficult to use these lipases to obtain modified oils and fats that meet the present purpose.
また、反応後の生成物については、ザラツキの原因成分
である対称型、2飽和モノオレイックトリグリセライド
が10%を越えると保存中にザラツキが早期に発生する
ため、このトリグリセライド含量を10%以下となるよ
うに調製する必要がある。また、生成物の33.3°C
以上での固体脂含量については、この値が2%を越える
と延展性、かたさ、0溶性などの点からソフトタイプの
マーガリンやショートニングに適さなくなるため、この
値を2%以下となるように反応を実施する必要がある。In addition, regarding the product after the reaction, if the symmetric type, disaturated monooleic triglyceride, which is the component that causes roughness, exceeds 10%, roughness will occur early during storage, so the triglyceride content should be kept below 10%. It is necessary to prepare it so that Also, the temperature of the product at 33.3°C
Regarding the solid fat content above, if this value exceeds 2%, it will not be suitable for soft type margarine or shortening in terms of spreadability, hardness, zero solubility, etc., so the reaction is carried out to keep this value below 2%. It is necessary to implement
以下に本発明を実施例に基づいて具体的に説明する。The present invention will be specifically described below based on Examples.
〔実施例−1〕
パーム油3.0kgと大豆油7.0kgを混合し60℃
で融解した。リゾラプス属由来の1. 3特異性を有す
る精製リパーゼ酵素製剤100gを時開64−2588
号に記載の方法に従い調製し、カラムに充填して、10
0 g/hrで通液した0反応温度は60°Cで実施し
、エステル交換生成物9.4kgを得た。得られた反応
生成物の分析値を表、1に示した。[Example-1] 3.0 kg of palm oil and 7.0 kg of soybean oil were mixed and heated to 60°C.
It melted. 1 from the genus Rhizolapus. 100g of purified lipase enzyme preparation with 3 specificities at 64-2588
Prepared according to the method described in No. 1, packed in a column,
The reaction temperature was 60°C with a flow rate of 0 g/hr, yielding 9.4 kg of transesterification product. The analytical values of the obtained reaction product are shown in Table 1.
これらの油脂を常法に従い精製処理した後オンレータ−
により、ガスを加えながら、急冷、練り合わせを行いシ
ョートニングを調製した。得られたショートニングは、
5. 10. 15“Cの各恒温槽に置き、ザラツキの
発現の有無を調べた0表。After refining these oils and fats according to conventional methods,
Shortening was prepared by rapidly cooling and kneading while adding gas. The obtained shortening is
5. 10. Table 0 was placed in each thermostat at 15"C and examined for the appearance of roughness.
(実施例−2〕
パーム油6kgと菜種油4kgを混合し、60°Cで融
解した。リゾラプス属由来の1.3特異性を有する精製
リパーゼ酵素製剤を用塾)、実施例−1の条件に従い、
エステル交換生成物を得た。得られた反応生成物の分析
値を表、3に示した。(Example-2) 6 kg of palm oil and 4 kg of rapeseed oil were mixed and melted at 60°C.A purified lipase enzyme preparation having 1.3 specificity derived from Rhizolapus was prepared according to the conditions of Example-1. ,
A transesterification product was obtained. The analytical values of the obtained reaction product are shown in Table 3.
これらの油脂を常法に従い精製処理した後オンレータ−
により、ガスを加えながら、急冷、練り合わせを行いシ
ョートニングを!I!l製した。得られたショートニン
グは、5. 10. 15℃の各恒温槽に置き、ザラツ
キの発現の有無を調べた0表。After refining these oils and fats according to conventional methods,
This allows shortening to be rapidly cooled and kneaded while adding gas! I! Made by l. The obtained shortening was prepared in 5. 10. Table 0 was placed in each thermostat at 15°C and examined for the appearance of roughness.
表。table.
〔実施例−3〕
パーム油5kgとコーン油5kgを混合し、60℃で融
解した。リゾラプス属由来の1.3特異性を有する精製
、リパーゼ酵素製剤を用い、実施例−1の条件に従い、
エステル交換生成物を得た。得られた反応生成物の分析
値を表、5に示した。[Example-3] 5 kg of palm oil and 5 kg of corn oil were mixed and melted at 60°C. Using a purified lipase enzyme preparation with 1.3 specificity derived from Rhizolapus genus and following the conditions of Example-1,
A transesterification product was obtained. The analytical values of the obtained reaction product are shown in Table 5.
これらの油脂を常法に従い精製処理し、(5)、(6)
の油m s、akgト:1− :/ 水ta脂(I V
63 ) 1.2kg、モノグリセライド50g、レ
シチン12g、β−カロチン12Bを60°Cで混合融
解する。一方、水層部として、水1.86kgに食塩1
40g、 粉乳120gを混合融解し、油層部に対し
て、この水層部を徐々に添加しながら撹拌機で予備乳化
する。この乳化物を更にポテータに通して急冷、練り合
わせを行いマーガリンを調整した。得られたマーガリン
は、冷蔵庫(5°C)に24時間保存して結晶の安定化
を行った後、5. 10. 15℃の各恒温槽に保存し
、ザラツキの発現の有無を調べた0表、6
実施例、 1. 2. 3は、保存後、6力月を経過
しても、ザラツキが確認されず、また性状も比較例に比
べ非常に良好であった。These oils and fats are purified according to conventional methods, (5), (6)
Oil m s, akg: 1-:/ Water tat (I V
63) Mix and melt 1.2 kg, monoglyceride 50 g, lecithin 12 g, and β-carotene 12B at 60°C. On the other hand, for the water layer, 1.86 kg of water and 1 salt
40 g of milk powder and 120 g of powdered milk are mixed and melted, and the aqueous layer is gradually added to the oil layer while pre-emulsification is carried out using a stirrer. This emulsion was further passed through a potator, rapidly cooled, and kneaded to prepare margarine. The obtained margarine was stored in a refrigerator (5°C) for 24 hours to stabilize the crystals, and then 5. 10. Table 0, 6 Examples, 1. Preserved in each thermostat at 15°C and examined for appearance of roughness. 2. In Sample No. 3, no roughness was observed even after 6 months of storage, and the properties were also very good compared to the comparative example.
表。table.
表。table.
表、 2
(発明の効果〕
実施例で示したように、本発明により得たられた改質油
脂をマーガリン、ショートニングに適用した場合、明ら
かに結晶性の改善が認められ、ザラツキの発現がなく、
また物性的にも非常に良好な製品が得られる。Table 2 (Effects of the Invention) As shown in the examples, when the modified oil and fat obtained by the present invention was applied to margarine and shortening, a clear improvement in crystallinity was observed, and no roughness appeared. ,
In addition, a product with very good physical properties can be obtained.
表。table.
Claims (2)
合油脂をリパーゼを用いてエステル交換することにより
、対称型、2飽和モノオレイックトリグリセライド含量
を10%以下、かつ33.3℃以上での固体脂含量を2
%以下含有することを特徴とするソフトタイプのマーガ
リン、ショートニング用改質油脂。(1) By transesterifying a mixed fat with edible fat containing at least 25% palm oil using lipase, the content of symmetrical, disaturated monooleic triglycerides is reduced to 10% or less, and at a temperature of 33.3°C or higher. Solid fat content 2
Modified fats and oils for soft type margarine and shortening, characterized by containing % or less.
ことを特徴とする特許請求範囲(1)記載のマーガリン
、ショートニング用改質油脂(2) Modified oil and fat for margarine and shortening according to claim (1), characterized in that a lipase with 1 or 3 specificity is used as the lipase.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1040673A JPH02219581A (en) | 1989-02-21 | 1989-02-21 | Modified fats and oils for margarine or shortening |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1040673A JPH02219581A (en) | 1989-02-21 | 1989-02-21 | Modified fats and oils for margarine or shortening |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02219581A true JPH02219581A (en) | 1990-09-03 |
Family
ID=12587048
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1040673A Pending JPH02219581A (en) | 1989-02-21 | 1989-02-21 | Modified fats and oils for margarine or shortening |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02219581A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996039855A1 (en) * | 1995-06-07 | 1996-12-19 | Unilever N.V. | Edible plastic spread |
EP0797921A2 (en) * | 1996-03-26 | 1997-10-01 | SHOWA SANGYO Co., Ltd. | Frying fat and oil |
US7927647B2 (en) | 2007-07-10 | 2011-04-19 | The Nisshin Oillio Group, Ltd. | Plastic fat composition |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6195098A (en) * | 1984-07-06 | 1986-05-13 | ユニリ−バ− ナ−ムロ−ゼ ベンノ−トシヤ−プ | Production of interesterified oils and fats |
-
1989
- 1989-02-21 JP JP1040673A patent/JPH02219581A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6195098A (en) * | 1984-07-06 | 1986-05-13 | ユニリ−バ− ナ−ムロ−ゼ ベンノ−トシヤ−プ | Production of interesterified oils and fats |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1996039855A1 (en) * | 1995-06-07 | 1996-12-19 | Unilever N.V. | Edible plastic spread |
EP0797921A2 (en) * | 1996-03-26 | 1997-10-01 | SHOWA SANGYO Co., Ltd. | Frying fat and oil |
EP0797921A3 (en) * | 1996-03-26 | 1999-03-10 | SHOWA SANGYO Co., Ltd. | Frying fat and oil |
US7927647B2 (en) | 2007-07-10 | 2011-04-19 | The Nisshin Oillio Group, Ltd. | Plastic fat composition |
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