IE47293B1 - Fat-liquoring process - Google Patents

Fat-liquoring process

Info

Publication number
IE47293B1
IE47293B1 IE1969/78A IE196978A IE47293B1 IE 47293 B1 IE47293 B1 IE 47293B1 IE 1969/78 A IE1969/78 A IE 1969/78A IE 196978 A IE196978 A IE 196978A IE 47293 B1 IE47293 B1 IE 47293B1
Authority
IE
Ireland
Prior art keywords
process according
oil
phosphatide
leather
liquoring
Prior art date
Application number
IE1969/78A
Other versions
IE781969L (en
Original Assignee
Unilever 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 Unilever Ltd filed Critical Unilever Ltd
Publication of IE781969L publication Critical patent/IE781969L/en
Publication of IE47293B1 publication Critical patent/IE47293B1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C14SKINS; HIDES; PELTS; LEATHER
    • C14CCHEMICAL TREATMENT OF HIDES, SKINS OR LEATHER, e.g. TANNING, IMPREGNATING, FINISHING; APPARATUS THEREFOR; COMPOSITIONS FOR TANNING
    • C14C9/00Impregnating leather for preserving, waterproofing, making resistant to heat or similar purposes
    • C14C9/02Impregnating leather for preserving, waterproofing, making resistant to heat or similar purposes using fatty or oily materials, e.g. fat liquoring

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Treatment And Processing Of Natural Fur Or Leather (AREA)

Abstract

of the Invention Hydroxylated phosphatides are used as component in or as the sole fattening agent in fat-liquoring. The hydroxylated phosphatide penetrates throughout the whole thickness of the leather, as opposed to non-modified phosphatides, giving the leather suppleness and softness. Rest fat content in the liquoring bath is low.

Description

The invention relates to a process for fat-liquoring tanned leather. In the technical process for converting hides and skin to leather, one of the steps is the fat-liquoring step. In this step the tanned leather is contacted with an aqueous emulsion of a fatty substance. After tanning, which serves to remove all undesirable substances from the leather, the leather is hard and stiff. The fat-liquoring serves to introduce a fatty substance into the fibre structure of the leather. The fatty substance has lubricating properties which impart to the leather suppleness, elasticity, strength and feel.
To fulfil the above functions, the fatty substance must be able to penetrate throughout the whole thickness of the leather and moreover he chemically or physically bound in the leather to prevent sweating out. To obtain this fixation, the fatty substance should contain polar groups.
The most used method for introducing the fatty substance is fat-liquoring. In this method the leather is contacted with an aqueous emulsion of the fatty substance. From an economical point of view it is also important that the leather should take up most of the fatty substance from the liquoring bath, i.e. the residual fat content of the liquor should be as low as possible to avoid undesirable losses.
As fatty substances sulphonated mineral, vegetable and animal oils are mostly used, often in admixture with nonsulphonated oils. Examples of such oils are Turkey red oil, sulphonated train oil, sulphonated sperm oil, neatsfoot oil, sulphonated fatty alcohols and also partially chlorinated, sulphonated or oxidised fats and fatty oils'.
In carrying out the fat-liquoring the leather is contacted at about 30 to 60°C with 100 to 200.% by weight of water containing 5 to 10% by weight of the fat,' both percentages being calculated cn the weight of the leather. The liquoring is continued until the maximum amount of fat has been taken up by the leather, which usually takes about 40 to 60 minutes.
It has been proposed (French Patent Specification 647/156) to use phosphatides in fat-liquoring because of its emulsifying properties and it was claimed that said phosphatides would assist in the penetration of the fat into the leather and would increase its fat uptake, However, in practice the use of phosph'atides in fat-liqupring has been very restricted, due to the fact that they are insufficiently taken up.-by the leather, leading to insufficient fattening of the interior of the leather. Such insufficient fatteniig leaves the leather too hard and too stiff. Moreover the poor fat uptake leads to high rest contents of fat in tne liquor and hence to high fat losses.
It has now beer found that' hydroxylated phosphatides are eminently suitable ior use as the fatty substance in fat liquors for fattening leather. In contrast to non-modified phosphatides, the hydroxylated phosphatides penetrate throughout the thickness of'the leather and they are almost completely taken up by the leather from the fat-liquor, making the rest content in the liquoring bath very low.
Therefore,the present invention provides a process for fat-liquoring tanned leather with an aqueous emulsion of a fatty substance comprising a phosphatide, which process is characterized iir that ai the phosphatide a hydroxylated phosphatide is used and the - fatty substance comprises 30 to 100% by weight,, more preferably 70 to luO% by weight of the hydroxylated phosphatide.
Preferably as the fatty substance a mixture of hydroxylated phosphatides is used, as obtained by hydroxylating a vegetable phosphatide mixture, separated from a vegetable oil, such as soyabean oil, peanut oil, rapeseed oil, cottonseed oil, etc. by a suitable degumming process; for instance by ‘0 treatment of the oil with water or steam. Especially soyabean phosphatides are being, preferred because of their general availability.
Further, phosphatides which before or after the hydroxylation have been modified in other ways can be used. Especi15 ally useful in this respect are phosphatides which before or after the hydroxylation have been subjected to a partial hydrolysis by treatment with an acid, a base or an enzyme, such as phospholipase A. Preferably, hydroxylated phosphatides are used which have been hydroxylated until the iO iodine value has decreased by 5 to 25%.
Also phosphatide fractions obtained by fractionation of crude or modified phosphatide mixtures with a solvent or a mixture of solvents may be used as the starting material for the hydroxylation; also the hydroxylated phosphatide mixture can be fractionated, and one or both of the fractions be used as the fattening agent- of the invention.
The fatty substance additionally may comprise oils which are customarily used in the art of fat-liquoring, such as neatsfoot oil, spenn oil, and/or sulphonated oil. Alternatively the fatty substance may contain soyabean oil.
For use with chromium-tanned leather it is desirable that the fattening mixture of the invention should contain a substance which increases its chromium resistance. As such substances ethoxylated alkyi phenols may be used, such as an ethoxylated nonyl phenol, available under the trade name Arkopal - N 150 (Arkopal is a Registered Trade Mark) frcm Farbwerke Ifoechst, Germany. When used, the amount of the chromium resistance increasing agent added is usually about 3 to 15% by weight, preferably 3 to 10%, and more preferably about 4 to 6(, calculated on the total fattening mixture. Also the salt stability of the fattening mixture is increased by such agents. Optionally an emulsifier may be added.
Process for hy< roxylating phosphatides are described in USP 2,445,948 and ii USP 2,629,662. In said process the phosphatides are re icted with an oxidising agent, preferably hydrogen peroxide, ipfcionally in the presence of an acid, such as acetic acid, however preferably lactic acid, serving as a catalyst. By + ie reaction double bonds contained in the fatty acid chains if the phosphatides are converted to glycolic hydroxyl r-’oups,some of which may be esterified with acyl groups. By this process the iodine value of the phosphatides is originally about 95 to 100, is decreased by 5 to 25%.
The phosphatid is fattening agents of the invention are used in substantially the same way as the fattening agents customarily used in fat-liquoring of leather, viz. in a rotating container the leather is contacted at 4o to 60°C with 100 to 200% by weight of water containing 5 to 10% by - 5 “ weight of the phosphatide fattening agent until the desired degree of fattening is reached.
The fattening agent of the invention can be used for fat-liquoring all kinds of leather, such as buckskin, split upper leather, vegetable tanned leather, grain leather, suede etc.
Example A number of chromium-tanned wet-blue cow hides were shaved to a thickness of 1.6 mm. The hides contained 5.9% CrgO-j, calculated on the dry matter, and their pH was 3.3.
The hides were brought into a rotating container and 200% by weight of water of 55°C was added. Then 2% by weight, calculated on the hides, of Tanigan PC (Tanigan is Registered Trade Hark) , (a tanning agent of Bayer, Germany) was added. After 10 minutes O.8S by weight of Luganilbraun NT (a dyestuff of BASF, Germany) dissolved in 15 times its weight of water was added, followed, after a further 10 minutes, by 6.3% by weight of a hydroxylated soyabean phosphatide mixture (iodine value 87-6 and containing 5% by weight of Arkopal-N 150, an ethoxylated nonyl phenol of Farbwerke Hoechst, Germany), dispersed in 7 times its weight of water. The temperature of the liquoring bath was 38°C and its pH %.72. After 20 minutes a mixture of 2% by weight of wattle, 2% by weight of Tanigan PR (a tanning agent of Bayer, Germany) and 2% by weight of Eetingan R7 (Retingan is a Trade Mark) (a tanning agent of Bayer, Germany) vzas added to the- bath. After 15 minutes 0.15% by weight of formic acid was added, and after a further 15 minutes the liquor was drained off. Next the hides were - 6 47293 washed with 400% by weight of water at 25°C‘for 10 minutes, whereafter the hides were allowed to drip dry overnight. Then the hides were pressed, vacuum-dried at 85°C for 2.5 minutes and post-dried at 25-30°C for 1.5 hours.
J After a few days the hides were staked.
After the fattening step the liquor contained only 0.95 g/l of the phosphatides. In view of the fact that 50% of the 200% of water added had been taken up by the hides, this means that 98% of the phosphatides had been taken up by the leather. The fattened hides contained 8.5% by weight of the phosphatides, calculated on the dryleather (determined by extraction with methylenechloride).
The physical properties of the fattened hides fulfilled all the requirements of a good quality sides leather.

Claims (12)

1. CLAIMS :1. A process for fat-liquoring tanned leather vzith an aqueous emulsion of a fatty substance comprising a phosphatide, which process is characterized in that as the phos5 phatide a hydroxyiated phosphatide is used and the fatty substance comprises 30 to 100% by weight of the hydroxyiated phosphatide.
2. Process according to claim 1, characterized in that a hydroxyiated vegetable phosphatide mixture is used. 10
3. A process according to claims 1 to 2, characterized in that hydroxyiated soyabean phosphatides are used.
4. Process according to claims 1 to 3, characterized in that a phosphatide is used which has been hydroxyiated until the iodine value has decreased by
5. To 25%. 15 5. Process according to any one of claims 1 to 4, characterized in that a partially hydrolysed, hydroxyiated phosphatide is used.
6. Process according to any one of claims 1 to 5, - 8 47293 characterized in that additionally a fatty oil and/or sulphonated oil, such as neatsfoot oil, sperm oil and sulphonated sperm oil, is used in the liquoring bath.
7. Process according to claim 6, characterized in that as the fatty oil soyabean oil is used.
8. Process according to any one of claims 1 to 7, characterized in that a chromium resistance improving agent is added.
9. Process according to claim 8, characterised in that as the chromium resistance improving agent an ethoxylated alkylphenol is used.
10. Process according to claim 9, characterized in that as the chromium resistance improving agent 3 to 15% by weight of an ethoxylated nonylphenol is used, calculated on the fatty substance.
11. Process according to any one of claims 1 to 10, characterized in that the liquoring bath contains an emulsifier.
12. Leather whenever treated according to a process as claimed in any one of claims 1 to 11.
IE1969/78A 1977-10-06 1978-10-02 Fat-liquoring process IE47293B1 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB4166877 1977-10-06

Publications (2)

Publication Number Publication Date
IE781969L IE781969L (en) 1979-04-06
IE47293B1 true IE47293B1 (en) 1984-02-08

Family

ID=10420760

Family Applications (1)

Application Number Title Priority Date Filing Date
IE1969/78A IE47293B1 (en) 1977-10-06 1978-10-02 Fat-liquoring process

Country Status (12)

Country Link
AR (1) AR214590A1 (en)
BE (1) BE871072A (en)
BR (1) BR7806651A (en)
CA (1) CA1102965A (en)
DE (1) DE2843755C3 (en)
DK (1) DK443578A (en)
FR (1) FR2405302A1 (en)
IE (1) IE47293B1 (en)
IT (1) IT1109569B (en)
NL (1) NL176277C (en)
SE (1) SE430793B (en)
ZA (1) ZA785627B (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE3238180C1 (en) * 1982-10-15 1984-04-19 Schill & Seilacher GmbH & Co, 7030 Böblingen Process for greasing leather and furs
DE3529073A1 (en) * 1984-08-22 1986-02-27 Sandoz-Patent-GmbH, 7850 Lörrach Preparations containing phosphoric acid partial esters, their preparation and their use
DE10207277A1 (en) * 2002-02-21 2003-09-04 Basf Ag Low-VOC greasing agents, their use in the production and / or treatment of leather and skins, and processes for the production and / or treatment of leather and skins with these greasing agents

Family Cites Families (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR642682A (en) * 1927-03-22 1928-09-01 Process for the preparation of special oils for buffing hides, wringing leathers, preparing rubble stone, etc.
DE514399C (en) * 1927-07-17 1930-12-11 Bruno Rewald Dr Preparations for greasing leather
FR647456A (en) * 1927-09-06 1928-11-24 Process for the manufacture of an ingredient which facilitates the tanning of leather
DE516187C (en) * 1927-09-07 1931-01-19 Bruno Rewald Dr Preparations for greasing leather
DE516188C (en) * 1927-10-25 1931-01-19 Bruno Rewald Dr Preparations for greasing leather
DE522041C (en) * 1927-12-06 1931-03-30 Bruno Rewald Dr Emulsifier for the production of an agent for greasing leather
DE516189C (en) * 1927-12-25 1931-01-19 Bruno Rewald Dr Preparations for greasing leather
GB306672A (en) * 1928-01-23 1929-02-28 Hanseatische Muehlenwerke Ag Improvements in or relating to processes for dressing leather, skins and the like
DE596576C (en) * 1928-08-21 1934-05-05 Oranienburger Chem Fab Akt Ges Fatliquor for leather
GB464100A (en) * 1935-10-08 1937-04-08 Bruno Rewald Improvements in and relating to phosphatide compositions
FR827822A (en) * 1936-10-21 1938-05-04 Chem Fab Gru Nau Landshoff & M Process and product for feeding leather
GB643403A (en) * 1940-05-11 1950-09-20 Nopco Chem Co Improvements relating to the production of blown fatty materials
US2445948A (en) * 1944-12-04 1948-07-27 Gen Mills Inc Hydroxyphosphatides
US2629662A (en) * 1948-06-17 1953-02-24 Glidden Co Process of treating phosphatides and product

Also Published As

Publication number Publication date
SE430793B (en) 1983-12-12
DE2843755B2 (en) 1980-07-31
IE781969L (en) 1979-04-06
AR214590A1 (en) 1979-06-29
IT7869326A0 (en) 1978-10-06
CA1102965A (en) 1981-06-16
BR7806651A (en) 1979-05-02
DE2843755C3 (en) 1981-03-12
BE871072A (en) 1979-04-06
IT1109569B (en) 1985-12-23
DK443578A (en) 1979-04-07
NL176277C (en) 1985-03-18
SE7810454L (en) 1979-04-07
DE2843755A1 (en) 1979-04-12
FR2405302A1 (en) 1979-05-04
NL7810085A (en) 1979-04-10
NL176277B (en) 1984-10-16
ZA785627B (en) 1980-05-28

Similar Documents

Publication Publication Date Title
US4762522A (en) Agent for treatment of hides and pelts
CA1102965A (en) Fat-liquoring process
US2158627A (en) Treatment of hides, skins, and leather
CA1129241A (en) Method of processing mechanically removed porcine skins for ultimate gelatin or leather production
KR20040094733A (en) Use of acrylic graft polymers in the field of collagen-based substrates and the substrates, skins and leathers thus obtained
US4281997A (en) Process for the greasing of leather and fur skins
US5476517A (en) Use of guerbet alcohols for preventing fatty spew on leather
US3749669A (en) Lubricants for hides and leather
KR100288734B1 (en) Leather processing method using alum
DE2802426C3 (en) Environmentally friendly and wastewater-free process for pickling, tanning and greasing fur skins
US2176434A (en) Lubricating of leather
EP0847453B1 (en) Process for the treatment of hides
Tournier Diagnosis, Prevention and Treatment of Fatty Spew
US3101238A (en) Fat liquoring with reaction product of epoxidized esters and polybasic inorganic acids
DE202074C (en)
Procter The making of leather
US1722398A (en) Process of tanning hides
Sugihartono et al. Extraction of fat/oil from fleshing by-product using a wet rendering process and combination with organic solvents
US3551089A (en) Ammonium zirconyl carbonate treatment of chrome-tanned leather
SU1370143A1 (en) Greasing composition
SU1266862A1 (en) Composition for fattening leather
SU1511279A1 (en) Composition for greasing hides
SU926013A1 (en) Composition for fat-liquoring skins
El Boushy et al. Hide and tanning waste by-products
WO2023057944A1 (en) Use of epoxidized vegetable oils as tanning agents