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GB2197337A - Hydrogenation of palm stearine - Google Patents
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GB2197337A - Hydrogenation of palm stearine - Google Patents

Hydrogenation of palm stearine Download PDF

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Publication number
GB2197337A
GB2197337A GB08627486A GB8627486A GB2197337A GB 2197337 A GB2197337 A GB 2197337A GB 08627486 A GB08627486 A GB 08627486A GB 8627486 A GB8627486 A GB 8627486A GB 2197337 A GB2197337 A GB 2197337A
Authority
GB
United Kingdom
Prior art keywords
palm
stearine
palm stearine
wax
tallow
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.)
Withdrawn
Application number
GB08627486A
Other versions
GB8627486D0 (en
Inventor
Tajchai Phadoemchit
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
BANGKOK REALTY CO Ltd
Original Assignee
BANGKOK REALTY CO 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 BANGKOK REALTY CO Ltd filed Critical BANGKOK REALTY CO Ltd
Priority to GB08627486A priority Critical patent/GB2197337A/en
Publication of GB8627486D0 publication Critical patent/GB8627486D0/en
Publication of GB2197337A publication Critical patent/GB2197337A/en
Withdrawn legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/12Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by hydrogenation

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  • Chemical & Material Sciences (AREA)
  • General 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)

Abstract

Palm stearine or a mixture of palm stearine and cow tallow is hydrogenated until the iodine value (IV) is in the range 1-5. The product may be used in making candles or match heads.

Description

SPECIFICATION Waxes from palm oils (palm stearine) This invention relates to producing wax from palm oil by hydrogenating palm stearine which is obtained from the thickened part of the palm oil until said palm oil is hard. It especially relates to producing wax from a mixture of palm oil and tallow (cow tallow) by mixing palm stearine with tallow then adding hydrogen until the mixture is homogeneous and hard at the desired melting point. This invention is useful for industrial uses either before or after deodourising, in the candles or matches industry and after deodourising, in the wax paper industry wherein it is used instead of petroleum oil. Wax from a mixture of palm oil and tallow is preferred because it is broken less and isles brittle than wax from palm oil only.
Palm stearine is a part of palm oil which is subjected to a fractionation process. There are two parts of the product, a transparent part is palm olein and a thickened part is palm stearine. Palm stearine is generally used in producing margarine, shortening, soap and animal food. The ratio of palm olein to palm stearine is about 65:35 parts. Because of commercial problems other products from wax are produced such as artificial wax for use in making candles, match heads, wax paper, etc.
Crude palm oil is subjected to degumming, bleaching, deodourisation and fractionation processes to produce palm stearine with the properties: iodine value (IV) =37-42 First melting point (MP) AOCS CC 3-25 =48-50 Melting point (MP) AOCS CC 1-25 =50-52 Though, in the case of palm stearine characteristics, the first melting point and melting point are rather high, they are not in accordance with the physiological properties whereby palm stearine is soft, is spreadable and is not rigid and so it is rather difficult to produce wax from the palm stearine.
The process for producing wax from palm stearine is hydrogenation of palm stearine comprising the following steps.
Palm stearine is melted by heating at about 60-70"C then pumped into a tank for addition of hydrogen, under a vacuum system and the vacuum is about 60 torr. Palm stearine is heated to 150"C and Ni Catalyst is added to the heated palm stearine in the ratio of 0. 1-0.3% by weight, and hydrogen is introduced into the tank and during the reaction the temperature rises to about 170-180"C. The hydrogen addition at the pressure of hydrogen of about 20-140 psi (137.,8-964.6 Kpa) is calculated on a theoretical basis. The product produced is evaluated periodically. When the reaction is stopped the iodine value from the analytical value is about 4.
The hydrogen addition is then stopped and the temperature lowered using a water cooling system to a temperature of about 90"C. The hydrogenated palm stearine is filtered to remove Ni-cataiyst. A comparison of non-hydrogenated palm stearine with the hydrogenated palm stearine is shown in Table 1 and a flow chart is shown in Fig. 1.
Table 1 Comparison of palm stearine before and after hydrogen addition.
Properties before H2 adding after H2 adding Iodine Value 37 - 42 1 - 5 mp 48 - 50 55 - 59 AOCS CC 3 - 25 mp 50 - 52 57 - 61 AOCS CC 1-25 Fatty acid composition BY GLC Lauric acid C12 0.3 - 0.5 0.3 - 0.5 Myristic acid C14 1.2 - 1.4 1.2 - 1.5 Palmitic acid C16 52 - 54 52 - 54 Stearic acid C18 3 - ; 42 42 - 44 Oleic acid 1801 31 - 33 Linoleic acid 1812 8 - 10 Linolenic acid C18l3 0.2 - 0.3 The product is hydrogenated palm stearine which has a little odour. It is particularly useful for (1) mixing with paraffin wax to make candles and (2) being a component for making match heads. If the product is subject to deodourisation process it is useful for (3) coating wax paper to prevent water percolation.
The hydrogenated palm stearine produced is brittle and it can be used effectively by mixing it with hydrogenated tallow (cow tallow). It can be mixed from 10,20,30,40 to 50% and each percentage of added hydrogenated tallow will reduce the brittleness of palm stearine. The properties are shown in Table 2.
For mixing with hydrogenated tallow, crude palm oil is treated in the same manner as above to obtain hydrogenated palm stearine, and the tallow is treated in the same manner as above to obtain hydrogenated, refined, bleached and deodourised tallow. The hydrogenated tallow is then mixed with the hydrogenated palm stearine until the iodine value is 1-5 preferably 1-2. The mixing is stopped and the product is filtered and deodourised especially when the product is to be used as composition ingredient of material for use in contact with edible products such as wax paper.
Palm steanne and tallow may be subjected to a purification process by adding alkali (NaOH) before being subjected in hydrogenation process, as shown in Fig. 2. Fig. 3 shows a flow chart for producing wax from an oil mixture.
Table 2 Properties Oil Mixture 1 Oil Mixture 2 Oil Mixture 3 Oil Mixture 4 Oil Mixture 5 Iodine Vlue 1-5 1-5 1-5 1-5 1-5 mp 55-62 55-62 55-62 55-62 55-62 (AOCS CC 3-25) mp 58-64 58-64 58-64 58-64 58-64 (AOCS CC 1-25) Fatty acid Composition by GLC Lauric acid C12 0.5-0.7 0.6-0.8 0.8-1.0 1.0-1.2 1.1-1.3 Myristic acid C14 1.5-1.7 1.6-1.9 2.0-2.2 2.1-2.4 2.4-2.6 Palmitic acid C16 50-51 46-49 44-47 42-44 40-42 Palmitoic acid C16.1 tr tr tr tr tr Stearic acid C18 44-46 46-48 48-50 50-52 51-54 Oleic acid C1811 tr tr tr tr tr Properties of wax from several ratio of palm stearine and tallow Oil mixture 1 Plam stearine and tallow ratio 90:10 hydrogenated Oil mixture 2 " 80:20 " Oil mixture 3 " 70:30 " Oil mixture 4 " 60:40 " Oil mixture 5 " 50:50 "

Claims (4)

1. A process for producing wax from palm oil which comprises adding hydrogen to palm stearine until the iodine value is in the range 1-5.
2. A process for producing wax from palm oil which comprises adding hydrogen to a mixture of palm stearine and tallow until the iodine value is in the range 1-5.
3. A process for producing wax from palm oil according to claim 1 or claim 2 substantially as hereinbefore described.
4. Wax whenever produced by the process according to any one of the preceding claims.
GB08627486A 1986-11-17 1986-11-17 Hydrogenation of palm stearine Withdrawn GB2197337A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
GB08627486A GB2197337A (en) 1986-11-17 1986-11-17 Hydrogenation of palm stearine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB08627486A GB2197337A (en) 1986-11-17 1986-11-17 Hydrogenation of palm stearine

Publications (2)

Publication Number Publication Date
GB8627486D0 GB8627486D0 (en) 1986-12-17
GB2197337A true GB2197337A (en) 1988-05-18

Family

ID=10607497

Family Applications (1)

Application Number Title Priority Date Filing Date
GB08627486A Withdrawn GB2197337A (en) 1986-11-17 1986-11-17 Hydrogenation of palm stearine

Country Status (1)

Country Link
GB (1) GB2197337A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4842648A (en) * 1987-10-22 1989-06-27 Tajchai Phadoemchit Paraffin wax replacer
FR2686349A1 (en) * 1991-10-09 1993-07-23 Lin Kuo Lung Method for the manufacture of a candle and wax composition employed
US6284007B1 (en) 1998-08-12 2001-09-04 Indiana Soybean Board, Inc. Vegetable lipid-based composition and candle
WO2001098445A1 (en) * 2000-06-21 2001-12-27 Binggrae Co., Ltd. Preventing flavor formation in hydrogenated vegetable oil
EP1776868A1 (en) * 2005-10-19 2007-04-25 Blyth, Inc. Container candle with mottled appearance
US7569084B2 (en) 1998-08-12 2009-08-04 Bernard Tao Vegetable lipid-based composition and candle
US20120189755A1 (en) * 2009-04-24 2012-07-26 Industria De Alimentos Zenu S.A.S. Pig-fat substitute based on vegetable fat and method for obtaining same
CN105008506A (en) * 2013-02-17 2015-10-28 埃莱万斯可再生能源科学股份有限公司 Effect of Wax Composition, and Metal on Burn Rate

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB816514A (en) * 1956-07-09 1959-07-15 Messrs J Bibby & Sons Ltd Improvements in or relating to a process for the production of an edible fat
GB920506A (en) * 1958-11-18 1963-03-06 Prosynthese Improvements in processes and apparatus for carrying out chemical reactions between gases and liquids
GB1441693A (en) * 1973-11-12 1976-07-07 Procter & Gamble Process for synthesizing specific complete mixed polyol esters
US4179454A (en) * 1978-07-24 1979-12-18 Scm Corporation Production of hydrogenated fatty acids from crude glyceride oils

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB816514A (en) * 1956-07-09 1959-07-15 Messrs J Bibby & Sons Ltd Improvements in or relating to a process for the production of an edible fat
GB920506A (en) * 1958-11-18 1963-03-06 Prosynthese Improvements in processes and apparatus for carrying out chemical reactions between gases and liquids
GB1441693A (en) * 1973-11-12 1976-07-07 Procter & Gamble Process for synthesizing specific complete mixed polyol esters
US4179454A (en) * 1978-07-24 1979-12-18 Scm Corporation Production of hydrogenated fatty acids from crude glyceride oils

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4842648A (en) * 1987-10-22 1989-06-27 Tajchai Phadoemchit Paraffin wax replacer
FR2686349A1 (en) * 1991-10-09 1993-07-23 Lin Kuo Lung Method for the manufacture of a candle and wax composition employed
US8137418B2 (en) 1998-08-12 2012-03-20 Indiana Soybean Alliance Vegetable lipid-based composition and candle
US8404003B2 (en) 1998-08-12 2013-03-26 Indiana Soybean Board, Inc. Vegetable lipid-based composition and candle
US6497735B2 (en) 1998-08-12 2002-12-24 Indiana Soybean Board Vegetable lipid-based composition and candle
US7569084B2 (en) 1998-08-12 2009-08-04 Bernard Tao Vegetable lipid-based composition and candle
US7731767B2 (en) 1998-08-12 2010-06-08 Indiana Soybean Board, Inc. Vegetable lipid-based composition and candle
US6284007B1 (en) 1998-08-12 2001-09-04 Indiana Soybean Board, Inc. Vegetable lipid-based composition and candle
WO2001098445A1 (en) * 2000-06-21 2001-12-27 Binggrae Co., Ltd. Preventing flavor formation in hydrogenated vegetable oil
EP1776868A1 (en) * 2005-10-19 2007-04-25 Blyth, Inc. Container candle with mottled appearance
US20120189755A1 (en) * 2009-04-24 2012-07-26 Industria De Alimentos Zenu S.A.S. Pig-fat substitute based on vegetable fat and method for obtaining same
CN105008506A (en) * 2013-02-17 2015-10-28 埃莱万斯可再生能源科学股份有限公司 Effect of Wax Composition, and Metal on Burn Rate
US11008532B2 (en) 2013-02-17 2021-05-18 Cargill, Incorporated Wax compositions and the effect of metals on burn rates
US11661566B2 (en) 2013-02-17 2023-05-30 Cargill, Incorporated Wax compositions and the effect of metals on burn rates
US12043819B2 (en) 2013-02-17 2024-07-23 Cargill, Incorporated Wax compositions and the effect of metals on burn rates
US12559698B2 (en) 2013-02-17 2026-02-24 Cargill, Incorporated Wax compositions and the effect of metals on burn rates

Also Published As

Publication number Publication date
GB8627486D0 (en) 1986-12-17

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Legal Events

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WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)
WAP Application withdrawn, taken to be withdrawn or refused ** after publication under section 16(1)