A kind of preparation method of environmentally friendly modified modified starch
Technical field
The invention belongs to chemical technology field, be specifically related to a kind of preparation method of environmentally friendly modified modified starch.
Background technology
Starch is that green plants passes through a kind of natural macromolecule carbohydrate that is comprised of a plurality of hydroxyl glucose units that photosynthesis generates.Starch and derivative resource thereof are very abundant, have that toxicity is low, readily biodegradable, can be degradable at occurring in nature, very friendly to environment, be widely used in a plurality of industrial circles such as food, weaving, papermaking, oil, building and medicine.Yet along with the development of industrial production technology, also more and more harsher to the requirement of starch property, ative starch has had a strong impact on its practical application effect because of the defective on its structure and performance.Therefore, developed the sex change technology of starch according to the formation and physic-chemical property of starch, Sumstar 190 is one of Some Important Modified Starches of early stage research, use.
Starch is Sumstar 190 with oxygenant effect products obtained therefrom in acid, alkali, neutral medium.Oxidizing reaction can not only make glycosidic link fracture, and also limitedly carbonylate and carboxyl on starch molecular chain drop to the retrogradation effect of amylose starch minimum, have greatly improved stability, film-forming properties, binding property and the transparency of sticking with paste liquid.Because Sumstar 190 has advantages of above-mentionedly, technique is simple, cheap in addition, therefore has a wide range of applications in the industry such as papermaking and weaving.
Adopt different oxidizing process, oxygenant and ative starch can make the different Sumstar 190 of performance, wherein the most frequently used, economical effectiveness again good oxygenant be mainly clorox and potassium permanganate.Use hypochlorite oxidation starch, cheap, though oxidation effectiveness is good, clorox is unstable, easily decomposites chlorine, and operator often feel dizzy due to the pollution of chlorine, has also increased requirement and the cost of sewage disposal aspect simultaneously; Use Potassium Permanganate as Oxidant, all be brown after under low pH value or high pH value condition, oxidized starch is being deposited for some time, had a strong impact on outward appearance and the result of use of product.So be badly in need of now a kind of oxygenant of effective, environmental protection.
Summary of the invention
The object of the invention is to, overcome the deficiencies in the prior art, a kind of preparation method of environmentally friendly modified modified starch is provided.Hydrogen peroxide is cheap, oxidisability is strong, usage quantity is less, can save production cost greatly.The more important thing is, adopt hydrogen peroxide oxidation starch not only can obtain the product of high purity, effect excellence, excessive hydrogen peroxide finally is decomposed into water, is a kind of comparatively desirable environmental protection oxygenant, greatly reduces the sewage disposal expense.
For solving the problems of the technologies described above, technical scheme of the present invention is: a kind of preparation method of environmentally friendly modified modified starch, and concrete steps are as follows:
(1) mix: at first prepare the starch emulsion that mass concentration is 30 ~ 38 %, add in mixing tank, start agitator, 0.1 ~ 20 % hydrogen peroxide oxidant that accounts for the catalytic reagent of 0.01 of starch oven dry weight ~ 0.5 ‰ and account for the starch oven dry weight is added in mixing tank and starch mixing 10-20 min;
(2) reaction of degeneration: after well-mixed material, conditioned reaction pH 3 ~ 11,30 ~ 55 ℃ of temperature of reaction, reaction times 1 ~ 5 h;
(3) neutralization reaction: after reaction 3 ~ 8 h, add reductive agent to stop oxidizing reaction; In adding and conditioning agent, make the pH value to 7.0 of final starch system ± 1.0;
(4) screening, weighing, packing: through the product of above-mentioned preparation, weighing and bagging gets final product after bolting.
Starch of the present invention is that one or more of corn, cassava, potato, wheat ative starch are arbitrarily than mixture.
Catalyzer in step of the present invention (1) is that one or more of copper sulfate, ferric sulfate, zinc sulfate are arbitrarily than mixture.
In step of the present invention (1), the mass concentration of hydrogen peroxide is 5 ~ 40 %.
In step of the present invention (2), one or more of regulating pH acid used when acid and be rare conditioning agent and be hydrochloric acid, sulfuric acid, phosphoric acid are arbitrarily than mixture, and mass concentration is 2 ~ 20 %; When regulating pH for alkalescence alkali used be one or more of sodium hydroxide, potassium hydroxide, sodium carbonate solution arbitrarily than mixture, mass concentration is 2 ~ 20 %.
In step of the present invention (3), reductive agent be one or more of Sodium Pyrosulfite, sodium bisulfite, S-WAT, Sulfothiorine arbitrarily than mixture, consumption is 0.05 of starch oven dry weight ~ 0.3 ‰.
In step of the present invention (3), in and conditioning agent be one or more of sodium hydroxide, potassium hydroxide, hydrochloric acid, sulfuric acid and phosphoric acid arbitrarily than mixture, mass concentration is 1 ~ 30 %.
The invention has the beneficial effects as follows: the present invention is not in the situation that increase facility investment, take hydrogen peroxide as oxygenant, add suitable catalyzer, just can make that in starch, the part reductibility end of the chain is oxidized to carboxyl, and the glucose unit of counting in 10 is just taken off in each reductibility end of the chain oxidation, simultaneously the new reductibility end of the chain appears again, until oxidation finishes.As long as suitably control the Sumstar 190 that oxidation depth just can obtain to suit the requirements.Preparation technology's advantages of simple of the present invention, low sticking, the high solid that make common ative starch have Sumstar 190 disperse the fundamental characteristics such as property and minimum gelification.In addition, also have several lower some advantage: (1) is compared with conventional hypochlorite oxidation starch, and the oxygenant consumption is few, and thermostability is strong, price is low, less investment; (2) the reaction decomposes product is water and oxygen, and environmental protection is conducive to further reduce cost of sewage disposal; (3) add catalyzer after, obvious Reaction time shorten, production efficiency is high, steady quality and energy consumption reduce greatly.
Embodiment
The below is further elaborated with reference to embodiment, but the present invention is not limited to these embodiment and using method.Experiment material used in following embodiment if no special instructions, all can be bought in routine biochemistry reagent shop; % in embodiment if no special instructions, is the quality percentage composition, and umber is mass parts.
Embodiment 1
Maize oxidized starch:
With 1000 parts of ative starchs and 1600 parts of water furnishing starch milks, add mixing tank, start mixing pump; Add the zinc sulfate of 0.01 % as catalyzer, the oxidant hydrogen peroxide (concentration is 20 %) that slowly adds 2 % that are equivalent to the ative starch over dry, regulate pH to 8.0 with the sodium hydroxide solution of 2 % again, begin to be warming up to 50 ℃, in the whole process of oxidizing reaction, keep pH between 8.0-8.5 always.When the starch emulsion temperature reaches 50 ℃, beginning timing oxidizing reaction 4 h.After reaction finishes, add the Sodium Pyrosulfite of 0.003 % of starch over dry with termination reaction, be neutralized to pH 7 left and right with 8 % hydrochloric acid.In oxidation reaction process, every 1 h sampling, detect viscosity, transmittance and thermostability, to control the various performances of product, reach and satisfy the user to the various service requirementss of Sumstar 190, sieve at last and pack to get the present invention's product.
Thermal stability data (take oxidation 2 h as example): first hour viscosity is as 11.3cp, and second hour viscosity is 10.9cp, and viscosity was 10.2cp in the 3rd hour; Thermostability=10.2 ÷ 11.3 * 100 %=90.26 %.
Embodiment 2
Cassava oxidized starch:
With 1000 parts of cassava ative starchs and 1600 parts of water furnishing starch milks, add mixing tank, start mixing pump; Add the ferric sulfate of 0.03 % as catalyzer, the oxidant hydrogen peroxide (concentration is 26 %) that slowly adds 0.5 % that is equivalent to the ative starch over dry, regulate pH to 4.0 with the hydrochloric acid soln of 6 % again, begin to be warming up to 35 ℃, in the whole process of oxidizing reaction, keep pH between 4.0-4.5 always.When the starch emulsion temperature reaches 35 ℃, beginning timing oxidizing reaction 5 h.After reaction finishes, add the S-WAT of 0.02 % of starch over dry with termination reaction, be neutralized to pH 7 left and right with 10 % sodium hydroxide.In oxidation reaction process, every 1 h sampling, detect viscosity, transmittance and thermostability etc., to control the various performances of product, reach and satisfy the user to the various service requirementss of Sumstar 190, sieve at last and pack to get the present invention's product.
Thermal stability data (take oxidation 3 h as example): viscosity was 21.8 cp in first hour, and second hour viscosity is 20.9 cp, and viscosity was 20.2 cp in the 3rd hour; Thermostability=20.2 ÷ 21.8 * 100 %=92.66 %.
Embodiment 3
Corn and potato mixed oxidization starch:
With 400 parts of native cornstarchs, 600 parts of potato ative starchs and 1600 parts of water furnishing starch milks, add mixing tank, start mixing pump; Add the copper sulfate of 0.01 % as catalyzer, slowly add 3% the oxidant hydrogen peroxide (concentration is 20 %) that is equivalent to the ative starch over dry, regulate pH to 8.0 with 4% sodium hydroxide solution again, begin to be warming up to 50 ℃, in the whole process of oxidizing reaction, keep pH between 7.0-7.5 always.When the starch emulsion temperature reaches 50 ℃, beginning timing oxidizing reaction 3h.After reaction finishes, add the Sodium Pyrosulfite of 0.002 % of starch over dry with termination reaction, be neutralized to pH 7 left and right with 15 % hydrochloric acid.In oxidation reaction process, every 1 h sampling, detect viscosity, transmittance and thermostability, to control the various performances of product, reach and satisfy the user to the various service requirementss of Sumstar 190, sieve at last and pack to get the present invention's product.
Thermal stability data (take oxidation 3 h as example): first hour viscosity is as 20.2cp, and second hour viscosity is 18.6 cp, and viscosity was 16.2cp in the 3rd hour; Thermostability=16.2 ÷ 20.2 * 100 %=80.20 %.