CN1775816A - Environment-protection low-consumption process for preparing chitin from shrimp shell and for extracting bioactivity substance - Google Patents
Environment-protection low-consumption process for preparing chitin from shrimp shell and for extracting bioactivity substance Download PDFInfo
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- CN1775816A CN1775816A CNA2005101014110A CN200510101411A CN1775816A CN 1775816 A CN1775816 A CN 1775816A CN A2005101014110 A CNA2005101014110 A CN A2005101014110A CN 200510101411 A CN200510101411 A CN 200510101411A CN 1775816 A CN1775816 A CN 1775816A
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Abstract
The invention discloses an environment protection low consume technique of making crust element from shrimp crust, and method of picking up bioactive substance that astaxanthin and biological calcium. The traditional crust element preparation method commonly adopts HCl decalcification, NaOH deproteinization, degrease. This can not utilize fully the high attachment value bioactive substance in the shrimp crust; and the discharged waste acid and lye contaminate the environment greatly. The invention adopts scientific method that while making crust element, the organic solvent is used to extract active substance astaxanthin; and the organic acid is used to do high value processing for the biological calcium to make into calcium nutrition-fruit acid calcium, at the same time do decalcification, extract animal protein powder. The advantages of the technique are that the environment protection contamination reaches the lowest; the consume are low; and the production value is high.
Description
Technical field the present invention relates to a kind ofly prepare the environment-protection low-consumption process of chitin from the shrimp shell, and extracts biologically active substance in preparation process---the method for astaxanthin and biological calcium.
The preparation method of the chitin that background technology is traditional generally all adopts the HCl decalcification, NaOH deproteinated, degreasing, the height that exists in the prawn shell is paid value added biologically active substance and is not carried out abundant extraction and application, and the spent acid waste lye serious environment pollution that discharges in the production process, and power consumption, water consumption.
Remove in the shrimp shell and contain materials such as chitin, protein, calcium, also contain astaxanthin.Chitin extensively is present in the shrimp and crab shells, and content accounts for 18%.Estimate that according to data the annual chitin that generates of occurring in nature has 10,000,000,000 tons approximately, in natural polymer, the storage capacity of chitin accounts for second, is only second to Mierocrystalline cellulose.In recent years, the research of chitin and derivative thereof is very active.Research contents includes the resource of chitin; the extraction of chitin, purifying; the analytical procedure of chitin and derivative thereof, structure determination and chitin comprise a plurality of subjects such as chemistry, environment protection, medical science, food, agricultural, biology, light industry in numerous Application for Field.Astaxanthin is the most a kind of xenthophylls that distributes in the animal kingdom, has unique colouring function, and generation that also can enhancing antibody strengthens the immunizing power of animal.Astaxanthin also is a kind of carotenoid additive that has potentiality, in food, feed, makeup, medicine and other fields wide prospect is arranged.At present, on the world market, astaxanthin costs an arm and a leg mainly as medical material and feed pigment, and market demand is very big.The astaxanthin of chemosynthesis accounts for about 90% of total sales volume, but countries in the world are to the management strictness of chemosynthesis astaxanthin, banned use of the astaxanthin of chemosynthesis as U.S. food and FAD (FAD), this shows that the exploitation natural astaxanthin has very big market potential and application prospect.
Summary of the invention the present invention adopts scientific and reasonable method in the preparation chitin, the active substance astaxanthin that contains in the shrimp shell is extracted, and the biological calcium that contains in the prawn shell is carried out high-valued processing, make current third generation calcium nutritious supplementary---calcium citrate malate, extract simultaneously and obtain animal albumen powder.This technology is reduced to environmental pollution minimum, and low consumption, Peak output.
The present invention realizes as follows:
(1) new fresh shrimp shell is cleaned, and dries, and 60 mesh sieves were pulverized in 50～60 ℃ of left and right sides forced air dryings then.With the nylon cloth bag of packing into of the shrimp shell after sieving, under 50～55 ℃, (solvent is: water/acetone=50～100/20～50/20～50 at 1mol/LNaOH solution, ml/ml/ml) soaked 8～24 hours in, the consumption of NaOH solution is: NaOH solution/shrimp shell=5～7/1 (ml/g), filter drying.
Contain a large amount of glutelins and astaxanthin in the filtrate.With the astaxanthin in the organic solvent extraction filtrate, organic solvent can be trichloromethane, methylene dichloride, ethyl acetate, the consumption of organic solvent is: solvent/filtrate=1～3/5 (ml/ml), extracting twice, separating and extracting liquid, organic solvent is reclaimed, can get the very high astaxanthin crude product of content, yield can reach 3～5g/kg.Extracting mother liquid transfers to pH=4～6 with dense HCl, makes protein precipitation, the separating, washing precipitation, and drying can get protein.Or add protease hydrolysis, the hydrolyzed solution evaporation concentration can be made the protolysate powder.
(2) with step (1) gained shrimp shell under 55～60 ℃, soaked again 8～24 hours with the 1mol/LNaOH aqueous solution, the consumption of the NaOH aqueous solution is: NaOH solution/shrimp shell=3～5/1 (ml/g) filter to dry.Filtrate is made into 1mol/LNaOH solution by the requirement of (1), waits until and handles next batch shrimp shell; Clean the shrimp shell to neutral, dry.
(3) contain good biological calcium in the shrimp shell, the mixed aqueous solution of step (2) gained shrimp shell usefulness citric acid and oxysuccinic acid is handled at 55～60 ℃ descended decalcification 8～24 hours.Filtering separation shrimp shell dries.The mol ratio of citric acid and oxysuccinic acid is in the nitration mixture aqueous solution: citric acid/oxysuccinic acid=2/3 (mol/mol).The consumption of nitration mixture is: nitration mixture/lime carbonate=70～80/20～30 (g/g) (general shrimp shell amount calciferous is about 30%); The mixed acid solution consumption is: mixed acid solution/shrimp shell=5～10/1 (ml/g).
With the refining evaporation concentration of filtrate, dry compressing tablet can make current third generation calcium nutritious supplementary---tartaric acid calcium tablet, and the general company standard of calcium citrate malate calcium content is: in Ca 190-210g/kg.
(4) step (3) shrimp shell was handled 8～24 hours down at 55～60 ℃ with the mixed aqueous solution of citric acid and oxysuccinic acid again, filtering separation shrimp shell dries.Filtrate is waited until and is handled next batch shrimp shell; Clean the shrimp shell to neutral, dry 50～60 ℃ of forced air dryings.Make chitin, deacetylation DD=25～30%.
(5) if the chitin that makes is used to produce chitosan, this operation of drying not, wet feed directly adds 45%NaOH solution (mass percentage concentration), handles 10～20 hours at 60～70 ℃, the alkali lye consumption is: alkali lye/shrimp shell=5～10/1 (ml/g), filter.Filtrate is made into the 1mol/LnaOH aqueous solution, is used for step (2). With newly joining 45%NaOH solution (mass percentage concentration), handled 10～20 hours at 60～70 ℃ more then, filtering separation shrimp shell dries, and is washed till neutrality, dries again, and 50～60 ℃ of forced air dryings obtain white chitosan finished product, deacetylation DD＞90%.
The alkali lye that is used for deacetylation is reusable: second step reusable 2 times of operation, be used for the first step operation then, and reuse again 2 times, (1) is mixed with the deproteinated of 1mol/LNaOH solution when being used for the shrimp shell and preparing chitin and handles then set by step.Because of the alkali lye that is used for deacetylation only contains a spot of ethanoyl, do not influence deproteinated, degreasing.
The embodiment embodiment of the invention:
New fresh shrimp shell is cleaned, and dries, and 60 mesh sieves were pulverized in 50～60 ℃ of left and right sides forced air dryings then.With the nylon cloth bag of packing into of the shrimp shell after sieving, under 50～55 ℃, (solvent is: water/acetone=50～100/20～50/20～50 at 1mol/LNaOH solution, ml/ml/ml) soaked 8～24 hours in, the consumption of NaOH solution is: NaOH solution/shrimp shell=5～7/1 (ml/g), filter drying.With the astaxanthin in the organic solvent extraction filtrate, organic solvent can be trichloromethane, methylene dichloride, ethyl acetate, and the consumption of organic solvent is: solvent/filtrate=1～3/5 (ml/ml), extracting twice, separating and extracting liquid reclaims organic solvent, makes the astaxanthin crude product.Extracting mother liquid transfers to pH=4～6 with dense HCl, makes protein precipitation, the separating, washing precipitation, and drying can get protein.Or add protease hydrolysis, the hydrolyzed solution evaporation concentration can be made the protolysate powder.
Gained shrimp shell was soaked under 55～60 ℃ 8～24 hours with the 1mol/LNaOH aqueous solution again, and the consumption of the NaOH aqueous solution is: NaOH solution/shrimp shell=3～5/1 (ml/g), filter drying.Filtrate is waited until and is handled next batch shrimp shell; Clean the shrimp shell, dry.Gained shrimp shell was handled 8～24 hours with the mixed aqueous solution of citric acid and oxysuccinic acid under 55～60 ℃, and filtering separation shrimp shell dries.The mol ratio of citric acid and oxysuccinic acid is in the nitration mixture aqueous solution: citric acid/oxysuccinic acid=2/3 (mol/mol).The consumption of nitration mixture is: nitration mixture/lime carbonate=70～80/20～30 (g/g) (general shrimp shell amount calciferous is about 30%); The mixed acid solution consumption is: mixed acid solution/shrimp shell=5～7/1 (ml/g).With the refining evaporation concentration of filtrate, dry compressing tablet can make current third generation calcium nutritious supplementary---tartaric acid calcium tablet, and gained calcium citrate malate calcium content is: in (the general company standard of calcium citrate malate calcium content is: in Ca 190-260g/kg) about Ca 250g/kg.
Gained shrimp shell was handled 8～24 hours down at 55～60 ℃ with the mixed aqueous solution of citric acid and oxysuccinic acid again, and filtering separation shrimp shell dries.Filtrate is waited until and is handled next batch shrimp shell; Clean the shrimp shell to neutral, dry 50～60 ℃ of forced air dryings.Make chitin, deacetylation DD=25～30%.
If the chitin that makes is used to produce chitosan, this operation of drying not, wet feed directly adds 45%NaOH (mass percentage concentration), handles 10～20 hours at 60～70 ℃, filters; And then with newly joining 45%NaOH, handled 10～20 hours at 60～70 ℃, be washed till neutrality, dry, 50～60 ℃ of forced air dryings obtain white chitosan finished product, deacetylation DD＞90%.
Claims (4)
1, a kind ofly preparing the environment-protection low-consumption process of chitin, chitosan and preparation process, extract biologically active substance from the shrimp shell---the method for astaxanthin and biological calcium is characterized in that described method comprises the steps:
(1) new fresh shrimp shell is cleaned, and dries, and 60 mesh sieves were pulverized in 50～60 ℃ of left and right sides forced air dryings then.With the nylon cloth bag of packing into of the shrimp shell after sieving, under 50～55 ℃, in 1mol/LNaOH solution, soaked 8～24 hours, filter, dry.Contain a large amount of glutelins and astaxanthin in the filtrate.With the astaxanthin in the organic solvent extraction filtrate, extracting twice, separating and extracting liquid, organic solvent is reclaimed, can get the very high astaxanthin crude product of content, yield can reach 3～5g/kg.Extracting mother liquid transfers to pH=4～6 with dense HCl, makes protein precipitation, the separating, washing precipitation, and drying can get protein.Or add protease hydrolysis, the hydrolyzed solution evaporation concentration can be made the protolysate powder.
(2) step (1) gained shrimp shell was soaked under 55～60 ℃ 8～24 hours with the 1mol/LNaOH aqueous solution again, the consumption of the NaOH aqueous solution is: NaOH solution/shrimp shell=3～5/1 (ml/g), filter drying.The filtrate requirement of (1) set by step is made into 1mol/LNaOH solution, waits until and handles next batch shrimp shell; Clean the shrimp shell to neutral, dry.
(3) with step (2) gained shrimp shell under 55～60 ℃, handled 8～24 hours with the mixed aqueous solution of citric acid and oxysuccinic acid, filtering separation shrimp shell dries.With the refining evaporation concentration of filtrate, dry compressing tablet can make current third generation calcium nutritious supplementary---tartaric acid calcium tablet.
(4) step (3) gained shrimp shell was handled 8～24 hours down at 55～60 ℃ with the mixed aqueous solution of citric acid and oxysuccinic acid again, filtering separation shrimp shell dries.Filtrate is waited until and is handled next batch shrimp shell; Clean the shrimp shell to neutral, dry 50～60 ℃ of forced air dryings.Make chitin, deacetylation DD=25～30%.
(5) if the chitin that makes is used to produce chitosan, this operation of drying not, wet feed directly adds 45%NaOH solution (mass percentage concentration), handles 10～20 hours at 60～70 ℃, the alkali lye consumption is: alkali lye/shrimp shell=5～10/1 (ml/g), filter.Filtrate is made into the 1mol/LnaOH aqueous solution, is used for step (2).And then with newly joining 45%NaOH solution (mass percentage concentration), handled 10～20 hours at 60～70 ℃, filter, be washed till neutrality, dry, 50～60 ℃ of forced air dryings obtain white chitosan finished product, deacetylation DD＞90%.
2, in accordance with the method for claim 1, it is characterized in that: described its solvent of 1mol/LNaOH solution is: water/acetone=50～100/20～50/20～50 (ml/ml/ml), the consumption of NaOH solution is: NaOH solution/shrimp shell=5～7/1 (ml/g).
3, in accordance with the method for claim 1, it is characterized in that: described organic solvent can be trichloromethane, methylene dichloride, ethyl acetate, and the consumption of organic solvent is: solvent/filtrate=1～3/5 (ml/ml).
4, in accordance with the method for claim 1, it is characterized in that: the mol ratio of citric acid and oxysuccinic acid is in the mixed aqueous solution of described citric acid and oxysuccinic acid: citric acid/oxysuccinic acid=2/3 (mol/mol).The consumption of nitration mixture is: nitration mixture/lime carbonate=70～80/20～30 (g/g) (general shrimp shell amount calciferous is about 30%); The mixed acid solution consumption is: mixed acid solution/shrimp shell=5～10/1 (ml/g).
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| CN102161714A (en) * | 2011-01-28 | 2011-08-24 | 上海海洋大学 | Process for preparing chitosan and calcium citrate |
| CN102219767A (en) * | 2011-04-27 | 2011-10-19 | 中国水产科学研究院南海水产研究所 | Method for preparing calcium ascorbate by utilizing shrimp shells |
| CN101560270B (en) * | 2009-06-09 | 2012-07-04 | 杨甫进 | Chitin production method with energy-saving and emission-reduction |
| CN102964467A (en) * | 2011-09-01 | 2013-03-13 | 湛江师范学院 | New process for preparing chitin |
| CN103404864A (en) * | 2013-08-26 | 2013-11-27 | 湖南农业大学 | Method for preparing calcium citrate malate from heads and shells of procambarus clarkii |
| CN103524641A (en) * | 2013-10-22 | 2014-01-22 | 扬州日兴生物科技股份有限公司 | Clean chitin production process with physical separation and biological enzymolysis |
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| CN105111330A (en) * | 2015-09-19 | 2015-12-02 | 吉林省蚕业科学研究院 | Process utilizing enzymatic removing impurity to prepare tussah pupa skin chitosan |
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