CN1673394A - Method for leather-making with Co2 supercritical fluid as medium - Google Patents
Method for leather-making with Co2 supercritical fluid as medium Download PDFInfo
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- CN1673394A CN1673394A CN 200510020464 CN200510020464A CN1673394A CN 1673394 A CN1673394 A CN 1673394A CN 200510020464 CN200510020464 CN 200510020464 CN 200510020464 A CN200510020464 A CN 200510020464A CN 1673394 A CN1673394 A CN 1673394A
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Abstract
The present invention provides one kind of tanning method with supercritical CO2 fluid as medium, and the tanning method adopts supercritical CO2 fluid as medium for at least one step of degreasing, enzyme depilation, softening, tanning, dyeing, fatting, etc. During the said operation, no entrainer is sued basically, and the treating course with supercritical CO2 fluid can lower the temperature to 33 deg.c, lower the pressure to 7.4 MPa, shorten the treating period to 60 min and decrease power consumption.
Description
Invention field
The present invention relates to a kind of is the method for leather-making of medium with the Co 2 supercritical fluid, and particularly, it is the method for leather-making of medium that the operation that the present invention relates to wherein lose hair or feathers adopts the Co 2 supercritical fluid of enzyme unhairing.
Background technology
Tanning industry is the important chemical industry, also is simultaneously the conventional industries that produce serious environmental pollution.The elimination tanning industry is polluted, and adopt pollutant control usually and clean two kinds of strategies of production technique, obviously, be the main method of fundamentally administering pollution with the production technique that cleans of abatement of pollution among production process.With the Co 2 supercritical fluid is the pollution-free tanning technology of medium, exactly a kind of novel method that proposes under this background.
Supercutical fluid (super critical fluids) technology is a chemical industry extracting and separating new technology that grows up near in the world more than ten years.CO wherein
2Isolating research of supercritical fluid extraction and application become one of main contents of this new technology.Supercutical fluid has the dissolving power near density of liquid and similar liquids, and the variation continuously with the variation of temperature and pressure of this dissolving power, and density is big more, and its dissolving power is strong more; Moreover, supercutical fluid also has near the viscosity of gas and velocity of diffusion, very high rate of mass transfer is arranged and reach the ability of extraction equilibrium very soon and very strong selectivity, and this is the major cause that supercutical fluid is better than common solvent.
The Co 2 supercritical fluid technology is mainly used in the extraction of aspects such as food, medicine and chemical industry and separates, as the extraction of edible rapeseed oil, soybean oil and sunflower seed oil; The extraction of pharmaceutical prod such as caffeine, amino acid etc.; Extract the Vanillin that can be used for makeup, beverage and flavouring agent production from wood pulp waste liquor, extract the bright-coloured natural food pigment of tone from hot red pepper, this natural pigment is widely used in the painted of beverage, candy, dessert, ice cream and cheese etc.Nineteen eighty-two has been held the symposium of " carbon dioxide solvent extraction and supercutical fluid chemistry and application " in Britain, held " supercutical fluid International Academic Exchange for the first time meeting " in October, 1988 at Nice, FRA, to the thermodynamics of supercutical fluid under the high pressure, comparatively comprehensively academic exchange has been carried out in the application of supercritical liquid extraction technique and supercritical fluid chromatography research and development.
The core of Co 2 supercritical fluid pollution-free tanning technology is to utilize the carbonic acid gas that is under the supercritical state to replace water as medium (or replacing some process hides chemical materials etc.), and implements " wet processing " technological process of process hides in this medium.This technology has proposed a kind of process hides new ideas of without sewage discharge.
The report that the co_2 supercritical fluid extraction isolation technique enters the leather industry field the earliest is in nineteen ninety-five.On the 23rd the international leather technology and Chemists Federation of holding in Germany May nineteen ninety-five, publish an article by people such as Carles and to have reported the degreasing experiment of Co 2 supercritical fluid pickling lamb skin and wet-white leather.It is fatty that this studies show that Co 2 supercritical fluid not only can be removed the remaining major part of intracutaneous in the degreasing of sheep pickled skin and wet-white leather, and more thorough to the removal of saturated fatty acid, Co 2 supercritical fluid also has stronger dehydration to pelt in addition.This research is used for the process hides degreasing process to the Co 2 supercritical fluid technology for the first time.
Though be used for the process hides degreasing about Co 2 supercritical fluid, tanning, dyeing, the more existing relevant reports of stuffing, but in these documents of being reported, generally must adopt entrainment agent, and its usage quantity reaches 10% of tare weight, this is a very big amount, entrainment agent comprises water and other organism, thereby must bring pollution, this makes that the advantage of CO 2 supercritical technology is weakened, in addition, the amount and the energy consumption of the process hides reagent that uses in the Co 2 supercritical fluid process hides process of having reported are relatively large, and this suitability for industrialized production for the Co 2 supercritical fluid tanning technology is also very unfavorable.Leather enzyme unhairing technology about in Co 2 supercritical fluid does not also have disclosed report.
Summary of the invention
The purpose of this invention is to provide a kind of Co 2 supercritical fluid that adopts is the method for leather-making of medium.Specifically, this method for leather-making be meant in traditional method for leather-making except that the immersion with water all wet manufacturing procedures as machining medium, change in the Co 2 supercritical fluid medium and implementing.
Therefore, this method comprises at least a of degreasing, enzyme unhairing, softening, tanning, dyeing and stuffing operation, if all adopt method of the present invention from degreasing to stuffing, except carrying out necessary mechanical epilation operation, all the other operations can realize continuous operation.For these reasons, the inventive method is self-evident at the beneficial effect aspect simplified processing process and shortening process-cycle.
Tanning operation in the inventive method, it is the well-known modern process hides operation in process hides field, use therein tanning agent is to buy various tanning agents by commercial sources, and these tanning agents can be listed for example chrome tanning agent, aluminum tanning agent, zirconium tanning agent, tannin extract, glutaraldehyde, synthetic tanning agent.But if the chrome tanning agent that adopts more traditional tanning agent for example to prepare voluntarily also need increase the operation of pickling procedure before tanning, this is the known technology in process hides field, and is when implementing the pickling operation with the inventive method, identical with the operational condition of conventional processes.
Substantially do not use entrainment agent when implementing the inventive method, and the amount and the energy consumption of the reagent that uses in Co 2 supercritical fluid process hides process are less relatively, the usage quantity of zymin is minimum in the Co 2 supercritical fluid treating processes is low to moderate 50 units/gram skins, temperature of reaction is reduced to 33 ℃, pressure is reduced to 9.0MPa, minimumly is low to moderate 7.4MPa.This suitability for industrialized production for the Co 2 supercritical fluid tanning technology is highly beneficial.The definite implication of above-described " not using entrainment agent basically " is, can not use entrainment agent, even use entrainment agent, its consumption also is no more than 3% of tare weight.For not being the entrainment agent that must use, method of the present invention does not have special requirement, and the known entrainment agent of prior art all can be used in the method for the present invention, for example water, methyl alcohol, ethanol, acetone, and wherein preferred water is as entrainment agent.
Details are as follows in concrete operations of the present invention, and wherein, except as otherwise noted, it is the weight percent of benchmark that all per-cents described in this specification sheets are with pending skin or leather weight.
Co 2 supercritical fluid tanning technology of the present invention can be widely used in various animal skin, mainly comprises ox-hide, pigskin, sheepskin etc., also can be used for the animal and plant protein of other form.Employed raw material skin is that fresh animal skin and/or process refrigerate, the animal skin of freezing, dry, salted method preservation.Except that fresh hide, the animal skin that additive method is preserved all will be through suitably handling, and makes it return to the fresh hide state and remove the additive that uses in the preservation process.The moisture content of the animal skin after the processing approaches the natural animal skin.Also can after water squeezing, carry out treatment with supercritical fluid, make moisture content in the skin significantly be lower than the level of natural animal skin, to guarantee in the course of processing, not having moisture to discharge.
The present invention does not have other special requirements for the device of this method of enforcement except that agitating function, so long as can carry out the known devices that Co 2 supercritical fluid is handled in the prior art, all can realize method of the present invention.Yet preferably, in view of the practical situation of opening the width of cloth and batch process of processed skin or leather, the device of implementing the inventive method should have enough big processing space and power.
Of the present invention is at least a of the degreasing that comprises the wet course of processing of process hides of the method for leather-making of medium, enzyme unhairing, softening, tanning, dyeing and stuffing operation with the Co 2 supercritical fluid.This method adopt with traditional technology substantially quite or the amount of less process hides reagent, do not use entrainment agent in operation substantially.This method is preferably at pressure: 7.4-10Mpa,, carry out Co 2 supercritical fluid of the present invention and handle by temperature: 33-40 ℃ under reaction times: 60-180 minute the condition.
The operation that available enzyme is handled in the inventive method comprises at least a of degreasing, enzyme unhairing and softening (enzymic hydrolysis).The used enzyme of above-mentioned enzyme treatment process is selected from aspartic protease, neutral protease or Sumizyme MP.Wherein, the used aspartic protease of enzyme treatment process can be at least a of stomach en-and 537 aspartic proteases, neutral protease can be at least a of Bacillus subtilus AS1.398 neutral protease, actinomycetes 166 neutral proteases, trypsinase and Quimotrase, and Sumizyme MP can be at least a of 209 Sumizyme MPs and 2709 Sumizyme MPs.
The present invention has significant spatter property and can economize on water.The efficient of enzyme significantly improves, and for example, common enzyme unhairing needs 200-400 units/gram skin, uses supercritical fluid technology only to need 50 units/gram skins; Speed of response is accelerated, and for example, under the conventional art condition, uses the dehairing process of banking up, and when the consumption of enzyme is 150 units/gram skins, when temperature was 35 ℃, the time of finishing enzyme unhairing was more than 48 hours, and under the condition of supercutical fluid, only needed 1 hour; Used carbonic acid gas is derived from nature, even discharging does not also produce chemical pollution, in fact, all right recycle of carbon dioxide; In addition, with low cost, basically eliminate of the present invention the use of water, topmost consumption is to be used for the electric energy that the adjustment of the compression of gas and system temperature consumes.Optimized technical scheme of the present invention makes temperature drop to 33 ℃, and pressure has dropped to below the 9.0MPa, the minimum 7.4MPa that reached, and the treatment time also significantly reduces, and this will make the energy consumption of system more reduce.
One ton of leather of every processing under present leather-making technology technical qualification, the general 100-150 ton tap water that consumes, China's leather output in 2004 is 500,000,000 square metres, uses about 2,500,000 tons of raw material skin, the water consumption of the course of processing is about hundred million tons of 2.5-3.75, and produces the sewage of same quantity.Use the present invention, have huge economy, environment and social benefit.
The present invention has the following advantages:
1. all chemical enginnering processes are all implemented in Co 2 supercritical fluid;
2. chemical technology whole process does not make water, does not produce sewage;
3. significantly reduced the use of Harmful chemicals, the sulfide that uses in traditional leather-making technology, lime, tensio-active agent, ammonium salt all are cancelled in the present invention;
4. do not use entrainment agent substantially, under some situation, the water that can use minute quantity is as entrainment agent, and effect can be better;
5. work simplification: traditional tanning chemistry technology is made up of tens step operations, and the present invention is reduced to the 2-3 step.Traditional degreasing, depilation, softening, multiple ash or the like operation is all merged into an operation; Pickling, tanning operation in the tradition process for tanning are reduced to simple tanning; Dyeing in the traditional technology and stuffing operation, merging is carried out.
Embodiment
Below with reference to embodiment the present invention is described further.
Embodiment one: CO
2Bacillus subtilus SA1.398 neutral protein enzyme unhairing, softening in the supercutical fluid
Feature: Bacillus subtilus SA1.398 neutral protease, 250 unit of activity/gram skin
Material:
Fresh porcine skin, neck
Bacillus subtilus SA1.398 neutral protease: 250 units/gram skins
Water: 2%
Time: total time: 285min, wherein reaction 150min degreasing, depilation, softening condition under 7.4-8.0Mpa pressure:
Temperature: 34 ℃-38 ℃, pressure: 7.4-8.0MPa, rotating speed: 48 rev/mins
Operation:
1. with the required water dissolution of required enzyme, drop into reactor with pigskin.About temperature adjustment to 35 ℃.Pressure: about 7.5MPa, rotate 150min.Release, be cooled to normal pressure, normal temperature, enzyme effect total time 285min;
2. machinery pushes away hair
The result:
1. reaction finishes to check: depilation is complete, and skin is pure white, can stay to refer to the trace seal;
2. inferior daily inspection: the hair eye enlarges, and there is slight mashed face the skin part.
Embodiment two: CO
2Bacillus subtilus SA1.398 neutral protein enzyme unhairing, softening in the supercutical fluid
Feature: Bacillus subtilus SA1.398 neutral protease, 200 units/gram skins
Material:
Salted pigskin, neck (backwater is to the fresh hide attitude),
Bacillus subtilus SA1.398 neutral protease: 200 units/gram skins
Water: 2%,
Time: total time 350min, wherein reaction 100min depilation, softening condition under 7.4-8.0MPa pressure:
34 ℃-36 ℃ of temperature, pressure: 7.4-8.0Mpa, rotating speed: 48 rev/mins
Operation:
1. drop into reactor with required water with required enzyme dissolving and with skin.Temperature adjustment to 35 ℃, pressure regulation are rotated 100min to the 7.5MPa.Release, be cooled to normal pressure, normal temperature,, enzyme effect total time 350min.
2. machinery pushes away hair
The result:
1. reaction finishes to check: epidermis, hair are sloughed clean, and skin is sliding, soft, pure white, can stay to refer to the trace seal;
2. inferior daily inspection: the slightly mashed face phenomenon of grain.
Embodiment three: CO
2Bacillus subtilus SA1.398 neutral protein enzyme unhairing, softening in the supercutical fluid
Feature: Bacillus subtilus SA1.398 neutral protease, 150 units/gram skins
Material:
Fresh porcine skin, neck
Bacillus subtilus SA1.398 neutral protease: 150 units/gram skins
Water: 2%
Time: total time 240min, wherein reaction 70min degreasing, depilation, softening condition under 7.5-8.0Mpa pressure:
Temperature: 35 ℃-36 ℃, pressure: 7.5-8.0Mpa, rotating speed: 48 rev/mins
Operation:
1. drop into reactor with required water with the dissolving of required enzyme and with skin, temperature adjustment to 35 ℃, pressure regulation power is rotated 70min to 7.8MPa, release, is cooled to normal pressure, normal temperature, enzyme effect total time 240min
2. machinery pushes away hair
The result:
1. reaction finishes to check: hair slightly firmly can be pulled up, and hair is tight, skin is harder;
2. inferior daily inspection: skin is hard, hair and epidermis can touch down,, grain is complete, and pore is clear substantially.
Embodiment four: CO
22709 basic protein enzyme unhairings, softening feature in the supercutical fluid: 2709 Sumizyme MPs, 150 unit of activity/gram skin
Material:
Fresh porcine skin, neck
2709 Sumizyme MPs: 150 units/gram skins
Water: 2%
Time: total time 315min, the wherein reaction 80min degreasing under 7.5-8.0Mpa pressure, depilation, softening condition:
Temperature: 34 ℃-36 ℃, pressure: 7.5-8.0Mpa, rotating speed: 48 commentaries on classics/min
Operation:
1. drop into reactor with required water with the dissolving of required enzyme and with skin, 34 ℃ of temperature adjustments, pressure regulation are rotated 80min to 7.8MPa, release, are cooled to normal temperature, normal pressure, enzyme effect total time 315min;
2. machinery pushes away hair
The result:
1. reaction finishes to check: pore is clear, and hair is tight, firmly can pull up;
2. inferior daily inspection: hair can be pulled up gently, and hair can push easily with epidermis.
Embodiment five: CO
2209 basic protein enzyme unhairings, softening feature in the supercutical fluid: alkaline enzyme: 150 unit of activity/gram skin
Material:
Pigskin, preceding the part between the ribs and the hips portion 209 Sumizyme MPs: 150 units/gram skins
Water: 2%
Time: total time 345min, wherein reaction 65min degreasing, depilation, softening condition under 7.5-8.0Mpa pressure:
Temperature: 33-35 ℃, pressure: 7.5-8.0Mpa, rotating speed: 58 commentaries on classics/min
Operation:
1. drop into reactor with required water with the dissolving of required enzyme and with skin, 34 ℃ of temperature adjustments, pressure regulation are rotated 65min to 7.8MPa, release, are cooled to normal temperature, normal pressure, enzyme effect total time 345min;
2. machinery pushes away hair
The result:
1. reaction finishes to check: hair can be pulled up gently, and pore is clear;
2. inferior daily inspection: local mashed face.
Embodiment six: CO
2Bacillus subtilus SA1.398 neutral protein enzyme unhairing, softening feature in the supercutical fluid: Bacillus subtilus SA1.398 neutral protease, 100 unit of activity/gram skin
Material:
Salted pigskin, abdomen back (backwater is to the fresh hide attitude) Bacillus subtilus SA1.398 neutral protease: 100 units/gram skins
Water: 2%
Time: total time 260min, wherein reaction 70min degreasing, depilation, softening condition under 7.6-8.0Mpa pressure:
Temperature: 35-40 ℃, pressure: 7.6-8.0Mpa, rotating speed: 54 commentaries on classics/min
Operation:
1. drop into reactor with required water with the dissolving of required enzyme and with skin, 36 ℃ of temperature adjustments, pressure regulation are rotated 70min to 7.8MPa, release, are cooled to normal temperature, normal pressure, enzyme effect total time 260min;
2. machinery pushes away hair.
The result:
1. reaction finishes to check: hair is tight, and it is difficult to pull up, and pore is clear;
2. inferior daily inspection: hair can push gently with epidermis, and skin is pure white, and grain is complete.
Embodiment seven: CO
2Bacillus subtilus SA1.398 neutral protein enzyme unhairing, softening in the supercutical fluid
Feature: Bacillus subtilus SA1.398 neutral protease: 50 unit of activity/gram skin
Material:
Fresh porcine skin, the part between the ribs and the hips portion
Bacillus subtilus SA1.398 neutral protease: 50 units/gram skins
Water: 2%
Time: total time 240min, wherein reaction 90min degreasing, depilation, softening condition under 7.5-7.8MPa pressure:
Temperature: 35-36 ℃, pressure: 7.5-7.8Mpa, rotating speed: 52 commentaries on classics/min
Operation:
1. drop into reactor with required water with the dissolving of required enzyme and with skin, 36 ℃ of temperature adjustments, pressure regulation are rotated 90min to 7.6MPa, release, are cooled to normal temperature, normal pressure, enzyme resultant action time 240min.
2. machinery pushes away hair
The result:
1. reaction finishes to check: hair is tight, almost can not pull up, and grain is complete;
2. inferior daily inspection: hair can push gently with epidermis, and pore is clear, and grain is complete.
Embodiment eight: CO
2Bacillus subtilus SA1.398 neutral protein enzyme unhairing, softening in the supercutical fluid
Feature: Bacillus subtilus SA1.398 neutral protease, 50 unit of activity/gram skin do not add water
Material:
Fresh porcine skin, the back
Bacillus subtilus SA1.398 neutral protease: 50 units/gram skins
Time: total time 275min, wherein reaction 60min degreasing, depilation, softening condition under 7.4-7.6MPa pressure:
Temperature: 33-34 ℃, pressure: 7.4-7.6Mpa, rotating speed: 50 commentaries on classics/min
Operation:
1. required enzyme is dropped into reactor with skin, 34 ℃ of temperature adjustments, pressure regulation be to 7.4MPa, rotates 60min, release, is cooled to normal temperature, normal pressure, enzyme resultant action time 275min;
2. machinery pushes away hair
The result:
1. reaction finishes to check: hair can be pulled up, and pore is clear;
2. inferior daily inspection: hair can push gently with epidermis, and pore is clear, and grain is complete.
Embodiment nine: CO
2Bacillus subtilus SA1.398 neutral protease degreasing under the normal pressure, depilation, softening
Feature: under normal temperature, the normal pressure, Bacillus subtilus SA1.398 neutral protease, 150 unit of activity/gram skin can not lose hair or feathers, soften
Material:
Salted pigskin, buttocks (backwater is to the fresh hide attitude) Bacillus subtilus SA1.398 neutral protease: 150 units/gram skins
Water: 2%
Time: total time 300min, wherein rotation time 70min
Degreasing, depilation, softening condition:
Temperature: normal temperature 32-35 ℃, pressure: normal pressure, rotating speed: 52 commentaries on classics/min
Operation:
With required enzyme with required water dissolution and evenly spreading upon on the flesh noodles of skin, throw skin and go into reactor, temperature adjustment to 35 ℃ feeds CO
2Gas rotates 70min, enzyme effect total time 300min
2. machinery pushes away hair
The result:
1. reaction finishes to check: hair is difficult to pull up, and pore is clear;
2. inferior daily inspection: most hairs still can't push, and do not have softening feature
Embodiment ten: CO
2Bacillus subtilus SA1.398 neutral protease degreasing in the supercutical fluid, depilation, softening feature: enzyme dosage is low, Bacillus subtilus AS1.398 neutral protease, 30 unit of activity/gram skin
Material:
Fresh porcine skin, buttocks Bacillus subtilus SA1.398 neutral protease: 30 units/gram skins
Water: 3%
Time: total time 325min, wherein reaction 60min degreasing, depilation, softening condition under 7.5-8.0MPa pressure:
Temperature: 36 ℃, pressure: 7.5-8.0Mpa, rotating speed: 50 commentaries on classics/min
Operation:
1. required enzyme is dropped into reactor with required water dissolution and with skin, 36 ℃ of temperature adjustments, pressure regulation be to 7.5MPa, rotates 60min, release, is cooled to normal temperature, normal pressure, enzyme resultant action time 325min
2. machinery pushes away hair
The result:
1. reaction finishes to check: firmly hair can be pulled up, and hair is tighter;
2. inferior daily inspection can easily be turned down hair and epidermis, and pore is clear, and skin is pure white, and grain is complete.
Embodiment 11: CO
2Goatskin degreasing in the supercutical fluid, enzyme unhairing, softening feature: Bacillus subtilus SA1.398 neutral protease, goatskin does not add water
Material:
Salted goatskin, belly (backwater is to the fresh hide attitude)
Bacillus subtilus AS1.398 neutral protease: 200 units/gram skins
Time: total time 325min, wherein reaction 70min degreasing, depilation, softening condition under 8.3-8.5MPa pressure:
Temperature: 35-37 ℃, pressure: 8.3-8.5MPa, rotating speed: 48 commentaries on classics/min
Operation:
1. required enzyme is dropped into reactor with skin, 36 ℃ of temperature adjustments, pressure regulation be to 8.5MPa, rotates 70min, release, is cooled to normal temperature, normal pressure, enzyme effect total time 325min;
2. machinery pushes away hair
The result:
1. reaction finishes to check: slightly firmly hair can be pulled up, and grain is complete
2. inferior daily inspection, the available push pedal of hair is touched down, and skin is pure white, and grain is complete, can stay to refer to the trace seal.
Embodiment 12: CO
2Degreasing in the supercutical fluid, depilation, softening and chrome tanning
Feature: degreasing, depilation, softening and two steps of chrome tanning carry out
Material:
The goat wet salted hide, belly (backwater is to the fresh hide state)
Bacillus subtilus SA1.398 neutral protease: 250 units/gram skins
Time: total time 315min, wherein reaction 85min degreasing, depilation, softening condition under 7.4-8.0MPa pressure:
Temperature: 35-37 ℃, pressure: 7.4-8.0MPa, rotating speed: 48 commentaries on classics/min
Operation:
1. required enzyme is dropped into reactor with required water dissolution and with skin, 36 ℃ of temperature adjustments, pressure regulation be to 8.0MPa, rotates 85min, release, is cooled to normal temperature, normal pressure, enzyme effect total time 315min;
2. mechanical epilation;
The result:
1. reaction finishes to check: hair can be pulled up, and grain is complete;
2. inferior daily inspection: hair can push, and the skin grain is pure white, can stay to refer to the trace seal.
Chrome tanning:
Sample: depilation back goatskin
Weigh: increase weight 30% as chrome tanning materials foundation by actual weight
Material:
(Pericarpium Citri tangerinae factory produces the C-2000 chromium powder, Cr
2O
3Content 21%, cloudy chromic compound, no basicity): 7%
Water: 2%
Time: total time 240min, wherein react 120min under 7.5-8.0Mpa pressure
Condition: temperature: 35-37 ℃, pressure: 7.5-8.0MPa, rotating speed: 50 rev/mins
Operation:
Required C-2000 chromium powder is dropped in the reactor with skin bit, and temperature adjustment to 37 ℃, pressure regulation are rotated 120min to 8.0MPa, release, are cooled to normal temperature, normal pressure, tanning effect total time 240min;
The result:
1. otch is checked the tanning effect: tan entirely, be even blue green inside and outside the leather;
2. shrinkage temperature is measured: measure in the water medium, do not shrink in the boiling water; Measure in the glycerine medium: 104 ℃ of shrinkage temperatures;
3. grain is smooth, color even.
Embodiment 13: CO
2Dyeing and fat-liquoring in the supercutical fluid
Sample: chrome tanning goatskin
Neutralization: liquor ratio 2, normal temperature (21 ℃), reaction times: 60 minutes
NaHCO
3?1％，NaAc?0.5％；
Terminal point pH is 6.2, mechanical dehydration after neutralization finishes;
The dyeing and stuffing condition: 37 ℃ of temperature, pressure 9.0MPa, 60 minutes time,
Erie black ATT:1%, direct fast black G:1%, sulfated oil negatively charged ion fatting agent: 18%, mix the back and add, dyeing and stuffing carries out simultaneously.
Operation: required dyestuff, fatting agent are dropped into reactor with skin bit, and increasing temperature and pressure to 37 ℃, 9.3MPa stirred 2.5 hours, discharge CO
2To normal pressure, end operation.
The result: dye on leather is even, the dyeing full impregnated, leather surface does not have unctuousness, and leather is half-dried attitude, no waste liquid, leather body softness, feel is good.
Embodiment 14: actinomycetes 166 neutral protein enzyme unhairings in the CO2 supercutical fluid
Feature: actinomycetes 166 neutral proteases, 100 units/gram skins
Sample: salted pigskin, buttocks (backwater is to the fresh hide attitude)
The depilation condition: 37 ℃ of temperature, pressure 9.3MPa, 2 hours depilation time,
Actinomycetes 166 neutral proteases: 100 units/gram skins
Operation: with embodiment ten;
The result: hair and epidermis touch and can remove, and skin is the dehydration attitude, and surface does not have greasy feeling, and grease is deposited on container bottom.
Embodiment 15: CO
2Deliming in the supercutical fluid
Feature: supercritical CO
2Deliming does not use other chemical reagent
Sample: liming pigskin, belly
Deliming condition: 37 ℃ of temperature, pressure 8.5MPa, 40 minutes time;
Operation: with embodiment ten;
The result: the phenolphthalein otch is checked colourless, and the expansion of skin descends, and surface does not have greasy feeling, and skin is the dehydration attitude.
Embodiment 16: CO
2Vegetable tanning in the supercutical fluid
Feature: vegetable tanning agent tanning
Sample is prepared: the pigskin that lost hair or feathers, belly
Method pickling is routinely spent the night, and terminal point pH is 3.5, mechanical then water squeezing;
The tanning condition: tamarack and myrica extract respectively are 25% of tare weight, 37 ℃ of temperature, and pressure 9.3MPa, 6 hours reaction times;
Operation: with embodiment ten;
The result: the appearance color uniformity, be dark-brown, leather is half-dried attitude, has loftiness, and tannin extract absorbs more complete; Otch is checked, full impregnated, and color even unanimity, shrinkage temperature are 80 ℃.
Claims (6)
1. with the Co 2 supercritical fluid method for leather-making of medium, wherein said Co 2 supercritical fluid is that the process hides of medium is the operation of carrying out at least one operation of degreasing, enzyme unhairing, softening, tanning, dyeing and stuffing operation in Co 2 supercritical fluid, it is characterized in that, when carrying out aforesaid operations, do not use entrainment agent substantially.
2. the method for claim 1 is characterized in that it is 7.4-10MPa that CO 2 supercritical is handled at pressure, and temperature is 33-40 ℃, and the reaction times is to carry out under 60-180 minute the condition.
3. claim 1 or 2 method is characterized in that at least one operation of degreasing, enzyme unhairing and softening process is used the enzyme that is selected from aspartic protease, neutral protease or Sumizyme MP.
4. the described method of claim 3 is characterized in that aspartic protease wherein is at least a of stomach en-and 537 aspartic proteases.
5. the described method of claim 3 is characterized in that used neutral protease is at least a of Bacillus subtilus AS1.398 neutral protease, actinomycetes 166 neutral proteases, trypsinase and Quimotrase,
6. the described method of claim 3 is characterized in that used Sumizyme MP is at least a of 209 Sumizyme MPs and 2709 Sumizyme MPs.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200510020464 CN1281766C (en) | 2005-03-07 | 2005-03-07 | Method for leather-making with Co2 supercritical fluid as medium |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200510020464 CN1281766C (en) | 2005-03-07 | 2005-03-07 | Method for leather-making with Co2 supercritical fluid as medium |
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| Publication Number | Publication Date |
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| CN1673394A true CN1673394A (en) | 2005-09-28 |
| CN1281766C CN1281766C (en) | 2006-10-25 |
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| CN 200510020464 Expired - Fee Related CN1281766C (en) | 2005-03-07 | 2005-03-07 | Method for leather-making with Co2 supercritical fluid as medium |
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Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102405297A (en) * | 2009-04-21 | 2012-04-04 | 德国弗劳恩霍夫应用研究促进协会 | Method for tanning animal skins |
| WO2015127935A1 (en) * | 2014-02-25 | 2015-09-03 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Method for tanning hides and tanned leather produced by means of said method |
| CN106244740A (en) * | 2016-08-30 | 2016-12-21 | 张玉斌 | A kind of employing supercritical CO2abstraction technique carries out the method for Corii Sus domestica defat |
| CN107142757A (en) * | 2017-05-27 | 2017-09-08 | 刘振 | A kind of leather non-aqueous dyeing method |
| CN110128569A (en) * | 2019-05-13 | 2019-08-16 | 东北农业大学 | A kind of extracting method of heparin sodium |
| CN113748242A (en) * | 2019-04-29 | 2021-12-03 | 伊科斯克有限公司 | Process for dyeing and/or retanning leather |
| CN113795599A (en) * | 2019-04-29 | 2021-12-14 | 伊科斯克有限公司 | Device for leather processing |
| CN116656888A (en) * | 2023-05-17 | 2023-08-29 | 烟台和壹博物馆有限公司 | Preparation method of environment-friendly leather, tanning agent composition and application thereof |
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2005
- 2005-03-07 CN CN 200510020464 patent/CN1281766C/en not_active Expired - Fee Related
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102405297A (en) * | 2009-04-21 | 2012-04-04 | 德国弗劳恩霍夫应用研究促进协会 | Method for tanning animal skins |
| CN102405297B (en) * | 2009-04-21 | 2014-02-12 | 德国弗劳恩霍夫应用研究促进协会 | Method for tanning animal skins |
| US9206486B2 (en) | 2009-04-21 | 2015-12-08 | Fraunhofer-Gesellschaft Zur Foerderung Der Angewandten Forschung E.V. | Method for tanning animal skins |
| WO2015127935A1 (en) * | 2014-02-25 | 2015-09-03 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Method for tanning hides and tanned leather produced by means of said method |
| CN106244740A (en) * | 2016-08-30 | 2016-12-21 | 张玉斌 | A kind of employing supercritical CO2abstraction technique carries out the method for Corii Sus domestica defat |
| CN107142757A (en) * | 2017-05-27 | 2017-09-08 | 刘振 | A kind of leather non-aqueous dyeing method |
| CN113748242A (en) * | 2019-04-29 | 2021-12-03 | 伊科斯克有限公司 | Process for dyeing and/or retanning leather |
| CN113795599A (en) * | 2019-04-29 | 2021-12-14 | 伊科斯克有限公司 | Device for leather processing |
| US20220220571A1 (en) * | 2019-04-29 | 2022-07-14 | Ecco Sko A/S | Method for dyeing and/or retanning of leather |
| CN110128569A (en) * | 2019-05-13 | 2019-08-16 | 东北农业大学 | A kind of extracting method of heparin sodium |
| CN116656888A (en) * | 2023-05-17 | 2023-08-29 | 烟台和壹博物馆有限公司 | Preparation method of environment-friendly leather, tanning agent composition and application thereof |
| CN116656888B (en) * | 2023-05-17 | 2024-05-14 | 烟台和壹博物馆有限公司 | Preparation method of environment-friendly leather, tanning agent composition and application thereof |
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| CN1281766C (en) | 2006-10-25 |
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