阅读说明：本技术 多功能降黏剂及制备方法 (Multifunctional viscosity reducer and preparation method thereof ) 是由 王平 季艳辉 于 2021-11-19 设计创作，主要内容包括：本发明属于降黏领域,尤其是一种多功能降黏剂及制备方法,针对现有的降黏率低、降黏率固定和难以裂解的问题,现提出如下方案,其多功能降黏剂按照质量份数计包括如下组分：20份的水、16份～20份的生物酶、6份～10份的壬基酚聚氧乙烯醚、6份～10份的氮杂卡宾铁、6份～10份的乙醇、2份～6份的改性混合料、2份～5份的添加剂和2份～5份的辅助剂,改性混合料包含改性后的纯碱和盐碱地浮土,可以有效对稠油进行分解,降低稠油的黏度,提升降黏剂的降黏率,而且随着温度的提升,可以有效地提升降黏率,保障对稠油的降黏效果,同时可以对稠油中的重质组分进行有效裂解,可以将稠油中大部分的重质组分裂解成轻质组分。(The invention belongs to the field of viscosity reduction, and particularly relates to a multifunctional viscosity reducer and a preparation method thereof, aiming at solving the problems of low viscosity reduction rate, fixed viscosity reduction rate and difficult cracking of the existing viscosity reducer, the following scheme is provided, wherein the multifunctional viscosity reducer comprises the following components in parts by mass: 20 parts of water, 16-20 parts of biological enzyme, 6-10 parts of nonylphenol polyoxyethylene ether, 6-10 parts of azacarbene iron, 6-10 parts of ethanol, 2-6 parts of modified mixture, 2-5 parts of additive and 2-5 parts of adjuvant, wherein the modified mixture comprises modified soda ash and saline-alkali soil floating soil, can effectively decompose the thickened oil, reduce the viscosity of the thickened oil and improve the viscosity reduction rate of the viscosity reducer, and can effectively improve the viscosity reduction rate along with the increase of temperature, ensure the viscosity reduction effect on the thickened oil, and can effectively crack heavy components in the thickened oil and crack most heavy components in the thickened oil into light components.)

1. The multifunctional viscosity reducer is characterized by comprising the following components in parts by weight: 20 parts of water, 16-20 parts of biological enzyme, 6-10 parts of nonylphenol polyoxyethylene ether, 6-10 parts of azacarbene iron, 6-10 parts of ethanol, 2-6 parts of modified mixture, 2-5 parts of additive and 2-5 parts of adjuvant, wherein the modified mixture comprises modified soda ash and floating soil of saline-alkali soil, the additive comprises composite straw powder, soda and coal, and the adjuvant comprises sulfur, argil, biological protein zinc and hypersalinity hard water.

2. The multifunctional viscosity reducer of claim 1, wherein the modification method of soda ash is as follows: mixing soda ash, ammonium nitrate and biological enzyme according to the proportion of 7:1:2, then adding the mixture into a reaction kettle, extracting air in the reaction kettle, controlling the temperature in the reaction kettle to be 125-135 ℃, reacting for 25-30 minutes, then injecting mixed gas into the reaction kettle, wherein the mixed gas comprises 50% of helium, 30% of neon and 20% of argon, reducing the temperature to 85-95 ℃, reacting for 35-45 minutes, then discharging the residual mixed gas, injecting air after the temperature in the reaction kettle is reduced to 45-60 ℃, naturally cooling to normal temperature, then pouring the mixture into grinding equipment for grinding until the powder passes through a 100-mesh sieve, and preparing the modified soda ash.

3. The multifunctional viscosity reducer according to claim 1, wherein the modification method of the floating soil of the saline-alkali soil comprises the following steps: adding 85% of floating soil of the saline-alkali soil, 10% of tributyl citrate and 5% of tungstate into high-salinity hard water, then adding the mixed solution into a reaction kettle, controlling the rotating speed of the reaction kettle to be 220 r/min-320 r/min, raising the temperature to 65-80 ℃, reacting for 25-35 minutes, then adding the solution into a dehydration container for heating, removing water in the mixture, drying, then placing into baking equipment for baking at 125-145 ℃, baking for 15-25 minutes in an anaerobic environment, and finally grinding to obtain the modified floating soil of the saline-alkali soil.

4. The multifunctional viscosity reducer according to claim 1, wherein the soda ash and the floating soil of the saline-alkali soil in the modified mixture are prepared according to the ratio of 40-60% to 40-60%, and the modified mixture is stored in a container at the temperature of 45-60 ℃ after being mixed.

5. The multifunctional viscosity reducer of claim 1, wherein the ratio of the composite straw powder to the soda to the coal in the additive is controlled to be 6.5:1.5:2, and the composite straw powder comprises wheat straw powder, rice straw powder, wheat bran powder, rice hull powder, peanut hull powder and corn straw powder.

6. The multifunctional viscosity reducer of claim 1, wherein the composite straw powder raw material is powder which is sieved by a 50-mesh sieve, the soda and coal raw materials are powder which is sieved by a 100-mesh sieve, and the finally prepared additive is sieved by the 50-mesh sieve.

7. The multifunctional viscosity reducer of claim 1, wherein the preparation method of the additive comprises the following steps: adding composite straw powder, soda, coal and water into a reaction container, then adding yeast, controlling the temperature of the reaction container to be 25-35 ℃, stirring while reacting, pouring the mixture into a reaction kettle after reacting for 6-7 hours, controlling the rotating speed to be 450-650 r/min, controlling the temperature to be 70-80 ℃, adding the mixture into a heating box after reacting for 5-15 minutes, heating for 15-25 minutes at 220-280 ℃, and finally grinding to obtain the additive.

8. The multifunctional viscosity reducer according to claim 1, wherein the auxiliary agent comprises sulfur, pottery clay, biological zinc proteinate and hypersalinity hard water at a ratio of 2.5:1.3:0.2:6, and the sulfur and the pottery clay are selected from powder materials with 20-50 meshes.

9. The multifunctional viscosity reducer of claim 1, wherein the preparation method of the auxiliary agent comprises the following steps: firstly adding argil into high-salinity hard water, stirring for 15-25 minutes at the rotating speed of 250-350 r/min, then adding sulfur and biological protein zinc, increasing the rotating speed to 450-650 r/min, increasing the temperature to 45-60 ℃, continuing to stir for 25-35 minutes, then drying and dehydrating to obtain particles, adding the particles into an oil bath kettle at 145-160 ℃ for heating, heating for 15-25 minutes, then immediately pouring the mixture into a container at 45 ℃ below zero for half an hour for cooling, taking out the mixture after cooling, and finally preparing the auxiliary agent.

10. The preparation method of the multifunctional viscosity reducing agent is characterized by comprising the following steps:

s1: adding nonylphenol polyoxyethylene ether and the modified mixture into a reaction kettle, raising the temperature of the reaction kettle to 55-65 ℃, controlling the rotating speed to be 250-350 r/min, and reacting for 5-15 minutes;

s2: adding azacarbene iron and biological enzyme, raising the temperature to 25-35 ℃, reacting for 5-10 minutes, adding water into the mixture, continuing to react for 15-25 minutes, and stopping heating to obtain a first solution;

s3: adding ethanol, an additive and an auxiliary agent into stirring equipment, keeping the interior of the stirring equipment in a vacuum state, raising the temperature to 65-75 ℃, and uniformly stirring to obtain a second solution;

s4: adding the second solution into the refrigerating chamber, cooling the second solution to minus 25 ℃, adding the second solution into the first solution, and rapidly stirring the solution to prepare a mixed solution;

s5: and adding the mixed solution into drying equipment for drying and dehydrating to finally prepare the multifunctional viscosity reducer.

Technical Field

The invention relates to the technical field of viscosity reduction, and particularly relates to a multifunctional viscosity reducer and a preparation method thereof.

Background

The thickened oil emulsifying viscosity reducer has the advantages of high viscosity, high condensation point, poor fluidity in stratum and the like, in order to ensure that the viscosity reducer is required to be used in normal production, the patent with the application number of CN201410553381.6 discloses a thickened oil emulsifying viscosity reducer.

However, the viscous oil emulsifying viscosity reducer has some problems, for example, the viscosity reducing effect is limited, only a small part of viscous oil can be effectively reduced, the viscosity reducing rate is low and relatively fixed, the viscosity reducing rate cannot be increased or decreased by changing the temperature, meanwhile, the heavy component in the viscous oil is difficult to crack, and only a small part of the heavy component in the viscous oil can be cracked into the light component.

Disclosure of Invention

Based on the problems of low viscosity reduction rate, relatively fixed viscosity reduction rate and low light component conversion rate in the background technology, the invention provides a multifunctional viscosity reducer and a preparation method thereof.

The multifunctional viscosity reducer comprises the following components in parts by weight: 20 parts of water, 16-20 parts of biological enzyme, 6-10 parts of nonylphenol polyoxyethylene ether, 6-10 parts of azacarbene iron, 6-10 parts of ethanol, 2-6 parts of modified mixture, 2-5 parts of additive and 2-5 parts of adjuvant, wherein the modified mixture comprises modified soda ash and floating soil of saline-alkali soil, the additive comprises composite straw powder, soda and coal, and the adjuvant comprises sulfur, argil, biological protein zinc and hypersalinity hard water.

Preferably, the modification method of the soda ash comprises the following steps: mixing soda ash, ammonium nitrate and biological enzyme according to the proportion of 7:1:2, then adding the mixture into a reaction kettle, extracting air in the reaction kettle, controlling the temperature in the reaction kettle to be 125-135 ℃, reacting for 25-30 minutes, then injecting mixed gas into the reaction kettle, wherein the mixed gas comprises 50% of helium, 30% of neon and 20% of argon, reducing the temperature to 85-95 ℃, reacting for 35-45 minutes, then discharging the residual mixed gas, injecting air after the temperature in the reaction kettle is reduced to 45-60 ℃, naturally cooling to normal temperature, then pouring the mixture into grinding equipment for grinding until the powder passes through a 100-mesh sieve, and preparing the modified soda ash.

Preferably, the modification method of the floating soil of the saline-alkali soil comprises the following steps: adding 85% of floating soil of the saline-alkali soil, 10% of tributyl citrate and 5% of tungstate into high-salinity hard water, then adding the mixed solution into a reaction kettle, controlling the rotating speed of the reaction kettle to be 220 r/min-320 r/min, raising the temperature to 65-80 ℃, reacting for 25-35 minutes, then adding the solution into a dehydration container for heating, removing water in the mixture, drying, then placing into baking equipment for baking at 125-145 ℃, baking for 15-25 minutes in an anaerobic environment, and finally grinding to obtain the modified floating soil of the saline-alkali soil.

Preferably, the soda ash and the saline-alkali soil are prepared according to the proportion of 40-60% to 40-60% in the modified mixture, and the modified mixture is stored in a container at the temperature of 45-60 ℃ after being mixed.

Preferably, the ratio of the composite straw powder, the soda and the coal in the additive is controlled to be 6.5:1.5:2, and the composite straw powder consists of wheat straw powder, rice straw powder, wheat bran powder, rice hull powder, peanut hull powder and corn straw powder.

Preferably, the raw material of the composite straw powder is powder which is sieved by a 50-mesh sieve, the raw materials of the soda and the coal are powder which is sieved by a 100-mesh sieve, and finally the prepared additive is sieved by the 50-mesh sieve.

Preferably, the preparation method of the additive comprises the following steps: adding composite straw powder, soda, coal and water into a reaction container, then adding yeast, controlling the temperature of the reaction container to be 25-35 ℃, stirring while reacting, pouring the mixture into a reaction kettle after reacting for 6-7 hours, controlling the rotating speed to be 450-650 r/min, controlling the temperature to be 70-80 ℃, adding the mixture into a heating box after reacting for 5-15 minutes, heating for 15-25 minutes at 220-280 ℃, and finally grinding to obtain the additive.

Preferably, the ratio of the sulfur to the argil to the biological zinc proteinate to the hypersalinity hard water in the adjuvant is 2.5:1.3:0.2:6, and the sulfur and the argil are powder materials which pass through 20-50 meshes.

Preferably, the preparation method of the adjuvant: firstly adding argil into high-salinity hard water, stirring for 15-25 minutes at the rotating speed of 250-350 r/min, then adding sulfur and biological protein zinc, increasing the rotating speed to 450-650 r/min, increasing the temperature to 45-60 ℃, continuing to stir for 25-35 minutes, then drying and dehydrating to obtain particles, adding the particles into an oil bath kettle at 145-160 ℃ for heating, heating for 15-25 minutes, then immediately pouring the mixture into a container at 45 ℃ below zero for half an hour for cooling, taking out the mixture after cooling, and finally preparing the auxiliary agent.

The preparation method of the multifunctional viscosity reducing agent comprises the following steps:

s1: adding nonylphenol polyoxyethylene ether and the modified mixture into a reaction kettle, raising the temperature of the reaction kettle to 55-65 ℃, controlling the rotating speed to be 250-350 r/min, and reacting for 5-15 minutes;

s2: adding azacarbene iron and biological enzyme, raising the temperature to 25-35 ℃, reacting for 5-10 minutes, adding water into the mixture, continuing to react for 15-25 minutes, and stopping heating to obtain a first solution;

s3: adding ethanol, an additive and an auxiliary agent into stirring equipment, keeping the interior of the stirring equipment in a vacuum state, raising the temperature to 65-75 ℃, and uniformly stirring to obtain a second solution;

s4: adding the second solution into the refrigerating chamber, cooling the second solution to minus 25 ℃, adding the second solution into the first solution, and rapidly stirring the solution to prepare a mixed solution;

s5: and adding the mixed solution into drying equipment for drying and dehydrating to finally prepare the multifunctional viscosity reducer.

The invention has the beneficial effects that:

the nonyl phenol polyoxyethylene ether, the azacarbene iron, the biological enzyme, the modified mixture, the additive and the auxiliary agent can effectively decompose the thick oil, the azacarbene iron can carry iron ion catalytic centers to disperse and permeate into a macromolecular association structure of heavy components of the thick oil, the catalytic activity of the viscosity reducer can be better exerted, the biological enzyme is also a catalyst, the biological enzyme can exert better effect after being matched with the nonyl phenol polyoxyethylene ether and the azacarbene iron, the modified mixture can further treat the nonyl phenol polyoxyethylene ether, the azacarbene iron and the biological enzyme, the activity of the thick oil is further stimulated, the additive and the auxiliary agent can enhance the dispersity and the activity of the viscosity reducer, the viscosity of the thick oil is reduced, the viscosity reducing rate of the viscosity reducer is improved, the viscosity reducing rate can be effectively improved along with the improvement of temperature, the viscosity reducing effect of the thick oil is ensured, and meanwhile, the heavy components in the thick oil can be effectively cracked, most heavy components in the thickened oil can be cracked into light components, and the environment-friendly performance of the viscosity reducer is improved due to the fact that biological materials are used more.

Drawings

Fig. 1 is a flow chart of the present invention.

Detailed Description

The present invention will be further illustrated with reference to the following specific examples.

Referring to FIG. 1, the first embodiment

The embodiment provides a multifunctional viscosity reducer, which comprises the following components in parts by mass: 20 parts of water, 18 parts of biological enzyme, 10 parts of nonylphenol polyoxyethylene ether, 9 parts of azacarbene iron, 8 parts of ethanol, 6 parts of modified mixture, 5 parts of additive and 5 parts of auxiliary agent, wherein the modified mixture comprises modified soda ash and floating soil of saline-alkali soil, the additive comprises composite straw powder, soda and coal, the auxiliary agent comprises sulfur, argil, zinc bioprotein and high-salinity hard water, and the modification method of the soda ash comprises the following steps: mixing soda ash, ammonium nitrate and biological enzyme according to the proportion of 7:1:2, then adding the mixture into a reaction kettle, extracting air in the reaction kettle, controlling the temperature in the reaction kettle to be 125-135 ℃, reacting for 25-30 minutes, then injecting mixed gas into the reaction kettle, wherein the mixed gas comprises 50% of helium, 30% of neon and 20% of argon, reducing the temperature to 85-95 ℃, reacting for 35-45 minutes, then discharging the residual mixed gas, injecting air after the temperature in the reaction kettle is reduced to 45-60 ℃, naturally cooling to normal temperature, then pouring the mixture into grinding equipment for grinding until the powder passes through a 100-mesh sieve, and preparing the modified soda ash, and the modification method of the floating soil of the saline-alkali soil comprises the following steps: adding 85% of saline-alkali soil float, 10% of tributyl citrate and 5% of tungstate into high-salinity hard water, then adding the mixed solution into a reaction kettle, controlling the rotation speed of the reaction kettle to be 220-320 r/min, raising the temperature to 65-80 ℃, reacting for 25-35 minutes, then adding the solution into a dehydration container for heating, removing water in the mixture, drying, then placing the mixture into a baking device for baking at 125-145 ℃, baking for 15-25 minutes in an oxygen-free environment, finally grinding to obtain the modified saline-alkali soil float, preparing the soda and the saline-alkali soil float according to the ratio of 40-60% to 40-60% in the modified mixture, storing the mixed modified mixture in a container at the temperature of 45-60 ℃, controlling the ratio of the composite straw powder, the soda and the coal in the additive to be 6.5:1.5:2, the composite straw powder consists of wheat straw powder, rice straw powder, wheat bran powder, rice hull powder, peanut hull powder and corn straw powder, the composite straw powder is prepared by selecting powder which is sieved by a 50-mesh sieve as raw materials, the soda and coal are prepared by selecting powder which is sieved by a 100-mesh sieve as raw materials, and finally the prepared additive is sieved by a 50-mesh sieve, and the preparation method of the additive comprises the following steps: adding composite straw powder, soda, coal and water into a reaction container, then adding yeast, controlling the temperature of the reaction container to be 25-35 ℃, stirring while reacting, pouring the mixture into a reaction kettle after reacting for 6-7 hours, controlling the rotating speed to be 450-650 r/min, controlling the temperature to be 70-80 ℃, adding the mixture into a heating box after reacting for 5-15 minutes, heating for 15-25 minutes at 220-280 ℃, and finally grinding to prepare an additive, wherein the ratio of sulfur, argil, biological protein zinc and high-salinity hard water in the auxiliary agent is 2.5:1.3:0.2:6, the sulfur and the argil are powder materials with 20-50 meshes, and the preparation method of the auxiliary agent comprises the following steps: firstly adding argil into high-salinity hard water, stirring for 15-25 minutes at the rotating speed of 250-350 r/min, then adding sulfur and biological protein zinc, increasing the rotating speed to 450-650 r/min, increasing the temperature to 45-60 ℃, continuing to stir for 25-35 minutes, then drying and dehydrating to obtain particles, adding the particles into an oil bath kettle at 145-160 ℃ for heating, heating for 15-25 minutes, then immediately pouring the mixture into a container at 45 ℃ below zero for half an hour for cooling, taking out the mixture after cooling, and finally preparing the auxiliary agent.

The preparation method of the multifunctional viscosity reducing agent comprises the following steps:

s1: adding nonylphenol polyoxyethylene ether and the modified mixture into a reaction kettle, raising the temperature of the reaction kettle to 55-65 ℃, controlling the rotating speed to be 250-350 r/min, and reacting for 5-15 minutes;

s2: adding azacarbene iron and biological enzyme, raising the temperature to 25-35 ℃, reacting for 5-10 minutes, adding water into the mixture, continuing to react for 15-25 minutes, and stopping heating to obtain a first solution;

s3: adding ethanol, an additive and an auxiliary agent into stirring equipment, keeping the interior of the stirring equipment in a vacuum state, raising the temperature to 65-75 ℃, and uniformly stirring to obtain a second solution;

s4: adding the second solution into the refrigerating chamber, cooling the second solution to minus 25 ℃, adding the second solution into the first solution, and rapidly stirring the solution to prepare a mixed solution;

s5: and adding the mixed solution into drying equipment for drying and dehydrating to finally prepare the multifunctional viscosity reducer.

Referring to FIG. 1, example II

The embodiment provides a multifunctional viscosity reducer, which comprises the following components in parts by mass: 20 parts of water, 16 parts of biological enzyme, 9 parts of nonylphenol polyoxyethylene ether, 9 parts of azacarbene iron, 9 parts of ethanol, 5 parts of modified mixture, 5 parts of additive and 4 parts of auxiliary agent, wherein the modified mixture comprises modified soda ash and floating soil of saline-alkali soil, the additive comprises composite straw powder, soda and coal, the auxiliary agent comprises sulfur, argil, zinc bioprotein and high-salinity hard water, and the modification method of the soda ash comprises the following steps: mixing soda ash, ammonium nitrate and biological enzyme according to the proportion of 7:1:2, then adding the mixture into a reaction kettle, extracting air in the reaction kettle, controlling the temperature in the reaction kettle to be 125-135 ℃, reacting for 25-30 minutes, then injecting mixed gas into the reaction kettle, wherein the mixed gas comprises 50% of helium, 30% of neon and 20% of argon, reducing the temperature to 85-95 ℃, reacting for 35-45 minutes, then discharging the residual mixed gas, injecting air after the temperature in the reaction kettle is reduced to 45-60 ℃, naturally cooling to normal temperature, then pouring the mixture into grinding equipment for grinding until the powder passes through a 100-mesh sieve, and preparing the modified soda ash, and the modification method of the floating soil of the saline-alkali soil comprises the following steps: adding 85% of saline-alkali soil float, 10% of tributyl citrate and 5% of tungstate into high-salinity hard water, then adding the mixed solution into a reaction kettle, controlling the rotation speed of the reaction kettle to be 220-320 r/min, raising the temperature to 65-80 ℃, reacting for 25-35 minutes, then adding the solution into a dehydration container for heating, removing water in the mixture, drying, then placing the mixture into a baking device for baking at 125-145 ℃, baking for 15-25 minutes in an oxygen-free environment, finally grinding to obtain the modified saline-alkali soil float, preparing the soda and the saline-alkali soil float according to the ratio of 40-60% to 40-60% in the modified mixture, storing the mixed modified mixture in a container at the temperature of 45-60 ℃, controlling the ratio of the composite straw powder, the soda and the coal in the additive to be 6.5:1.5:2, the composite straw powder consists of wheat straw powder, rice straw powder, wheat bran powder, rice hull powder, peanut hull powder and corn straw powder, the composite straw powder is prepared by selecting powder which is sieved by a 50-mesh sieve as raw materials, the soda and coal are prepared by selecting powder which is sieved by a 100-mesh sieve as raw materials, and finally the prepared additive is sieved by a 50-mesh sieve, and the preparation method of the additive comprises the following steps: adding composite straw powder, soda, coal and water into a reaction container, then adding yeast, controlling the temperature of the reaction container to be 25-35 ℃, stirring while reacting, pouring the mixture into a reaction kettle after reacting for 6-7 hours, controlling the rotating speed to be 450-650 r/min, controlling the temperature to be 70-80 ℃, adding the mixture into a heating box after reacting for 5-15 minutes, heating for 15-25 minutes at 220-280 ℃, and finally grinding to prepare an additive, wherein the ratio of sulfur, argil, biological protein zinc and high-salinity hard water in the auxiliary agent is 2.5:1.3:0.2:6, the sulfur and the argil are powder materials with 20-50 meshes, and the preparation method of the auxiliary agent comprises the following steps: firstly adding argil into high-salinity hard water, stirring for 15-25 minutes at the rotating speed of 250-350 r/min, then adding sulfur and biological protein zinc, increasing the rotating speed to 450-650 r/min, increasing the temperature to 45-60 ℃, continuing to stir for 25-35 minutes, then drying and dehydrating to obtain particles, adding the particles into an oil bath kettle at 145-160 ℃ for heating, heating for 15-25 minutes, then immediately pouring the mixture into a container at 45 ℃ below zero for half an hour for cooling, taking out the mixture after cooling, and finally preparing the auxiliary agent.

The preparation method of the multifunctional viscosity reducing agent comprises the following steps:

s1: adding nonylphenol polyoxyethylene ether and the modified mixture into a reaction kettle, raising the temperature of the reaction kettle to 55-65 ℃, controlling the rotating speed to be 250-350 r/min, and reacting for 5-15 minutes;

s2: adding azacarbene iron and biological enzyme, raising the temperature to 25-35 ℃, reacting for 5-10 minutes, adding water into the mixture, continuing to react for 15-25 minutes, and stopping heating to obtain a first solution;

s3: adding ethanol, an additive and an auxiliary agent into stirring equipment, keeping the interior of the stirring equipment in a vacuum state, raising the temperature to 65-75 ℃, and uniformly stirring to obtain a second solution;

s4: adding the second solution into the refrigerating chamber, cooling the second solution to minus 25 ℃, adding the second solution into the first solution, and rapidly stirring the solution to prepare a mixed solution;

s5: and adding the mixed solution into drying equipment for drying and dehydrating to finally prepare the multifunctional viscosity reducer.

Referring to FIG. 1, example III

The embodiment provides a multifunctional viscosity reducer, which comprises the following components in parts by mass: 20 parts of water, 18 parts of biological enzyme, 7 parts of nonylphenol polyoxyethylene ether, 8 parts of azacarbene iron, 8 parts of ethanol, 6 parts of modified mixture, 4 parts of additive and 4 parts of auxiliary agent, wherein the modified mixture comprises modified soda ash and floating soil of saline-alkali soil, the additive comprises composite straw powder, soda and coal, the auxiliary agent comprises sulfur, argil, zinc bioprotein and high-salinity hard water, and the modification method of the soda ash comprises the following steps: mixing soda ash, ammonium nitrate and biological enzyme according to the proportion of 7:1:2, then adding the mixture into a reaction kettle, extracting air in the reaction kettle, controlling the temperature in the reaction kettle to be 125-135 ℃, reacting for 25-30 minutes, then injecting mixed gas into the reaction kettle, wherein the mixed gas comprises 50% of helium, 30% of neon and 20% of argon, reducing the temperature to 85-95 ℃, reacting for 35-45 minutes, then discharging the residual mixed gas, injecting air after the temperature in the reaction kettle is reduced to 45-60 ℃, naturally cooling to normal temperature, then pouring the mixture into grinding equipment for grinding until the powder passes through a 100-mesh sieve, and preparing the modified soda ash, and the modification method of the floating soil of the saline-alkali soil comprises the following steps: adding 85% of saline-alkali soil float, 10% of tributyl citrate and 5% of tungstate into high-salinity hard water, then adding the mixed solution into a reaction kettle, controlling the rotation speed of the reaction kettle to be 220-320 r/min, raising the temperature to 65-80 ℃, reacting for 25-35 minutes, then adding the solution into a dehydration container for heating, removing water in the mixture, drying, then placing the mixture into a baking device for baking at 125-145 ℃, baking for 15-25 minutes in an oxygen-free environment, finally grinding to obtain the modified saline-alkali soil float, preparing the soda and the saline-alkali soil float according to the ratio of 40-60% to 40-60% in the modified mixture, storing the mixed modified mixture in a container at the temperature of 45-60 ℃, controlling the ratio of the composite straw powder, the soda and the coal in the additive to be 6.5:1.5:2, the composite straw powder consists of wheat straw powder, rice straw powder, wheat bran powder, rice hull powder, peanut hull powder and corn straw powder, the composite straw powder is prepared by selecting powder which is sieved by a 50-mesh sieve as raw materials, the soda and coal are prepared by selecting powder which is sieved by a 100-mesh sieve as raw materials, and finally the prepared additive is sieved by a 50-mesh sieve, and the preparation method of the additive comprises the following steps: adding composite straw powder, soda, coal and water into a reaction container, then adding yeast, controlling the temperature of the reaction container to be 25-35 ℃, stirring while reacting, pouring the mixture into a reaction kettle after reacting for 6-7 hours, controlling the rotating speed to be 450-650 r/min, controlling the temperature to be 70-80 ℃, adding the mixture into a heating box after reacting for 5-15 minutes, heating for 15-25 minutes at 220-280 ℃, and finally grinding to prepare an additive, wherein the ratio of sulfur, argil, biological protein zinc and high-salinity hard water in the auxiliary agent is 2.5:1.3:0.2:6, the sulfur and the argil are powder materials with 20-50 meshes, and the preparation method of the auxiliary agent comprises the following steps: firstly adding argil into high-salinity hard water, stirring for 15-25 minutes at the rotating speed of 250-350 r/min, then adding sulfur and biological protein zinc, increasing the rotating speed to 450-650 r/min, increasing the temperature to 45-60 ℃, continuing to stir for 25-35 minutes, then drying and dehydrating to obtain particles, adding the particles into an oil bath kettle at 145-160 ℃ for heating, heating for 15-25 minutes, then immediately pouring the mixture into a container at 45 ℃ below zero for half an hour for cooling, taking out the mixture after cooling, and finally preparing the auxiliary agent.

The preparation method of the multifunctional viscosity reducing agent comprises the following steps:

s1: adding nonylphenol polyoxyethylene ether and the modified mixture into a reaction kettle, raising the temperature of the reaction kettle to 55-65 ℃, controlling the rotating speed to be 250-350 r/min, and reacting for 5-15 minutes;

s2: adding azacarbene iron and biological enzyme, raising the temperature to 25-35 ℃, reacting for 5-10 minutes, adding water into the mixture, continuing to react for 15-25 minutes, and stopping heating to obtain a first solution;

s3: adding ethanol, an additive and an auxiliary agent into stirring equipment, keeping the interior of the stirring equipment in a vacuum state, raising the temperature to 65-75 ℃, and uniformly stirring to obtain a second solution;

s4: adding the second solution into the refrigerating chamber, cooling the second solution to minus 25 ℃, adding the second solution into the first solution, and rapidly stirring the solution to prepare a mixed solution;

s5: and adding the mixed solution into drying equipment for drying and dehydrating to finally prepare the multifunctional viscosity reducer.

Referring to FIG. 1, example No. four

The embodiment provides a multifunctional viscosity reducer, which comprises the following components in parts by mass: 20 parts of water, 16 parts of biological enzyme, 8 parts of nonylphenol polyoxyethylene ether, 7 parts of azacarbene iron, 6 parts of ethanol, 3 parts of modified mixture, 3 parts of additive and 2 parts of auxiliary agent, wherein the modified mixture comprises modified soda ash and floating soil of saline-alkali soil, the additive comprises composite straw powder, soda and coal, the auxiliary agent comprises sulfur, argil, zinc bioprotein and high-salinity hard water, and the modification method of the soda ash comprises the following steps: mixing soda ash, ammonium nitrate and biological enzyme according to the proportion of 7:1:2, then adding the mixture into a reaction kettle, extracting air in the reaction kettle, controlling the temperature in the reaction kettle to be 125-135 ℃, reacting for 25-30 minutes, then injecting mixed gas into the reaction kettle, wherein the mixed gas comprises 50% of helium, 30% of neon and 20% of argon, reducing the temperature to 85-95 ℃, reacting for 35-45 minutes, then discharging the residual mixed gas, injecting air after the temperature in the reaction kettle is reduced to 45-60 ℃, naturally cooling to normal temperature, then pouring the mixture into grinding equipment for grinding until the powder passes through a 100-mesh sieve, and preparing the modified soda ash, and the modification method of the floating soil of the saline-alkali soil comprises the following steps: adding 85% of saline-alkali soil float, 10% of tributyl citrate and 5% of tungstate into high-salinity hard water, then adding the mixed solution into a reaction kettle, controlling the rotation speed of the reaction kettle to be 220-320 r/min, raising the temperature to 65-80 ℃, reacting for 25-35 minutes, then adding the solution into a dehydration container for heating, removing water in the mixture, drying, then placing the mixture into a baking device for baking at 125-145 ℃, baking for 15-25 minutes in an oxygen-free environment, finally grinding to obtain the modified saline-alkali soil float, preparing the soda and the saline-alkali soil float according to the ratio of 40-60% to 40-60% in the modified mixture, storing the mixed modified mixture in a container at the temperature of 45-60 ℃, controlling the ratio of the composite straw powder, the soda and the coal in the additive to be 6.5:1.5:2, the composite straw powder consists of wheat straw powder, rice straw powder, wheat bran powder, rice hull powder, peanut hull powder and corn straw powder, the composite straw powder is prepared by selecting powder which is sieved by a 50-mesh sieve as raw materials, the soda and coal are prepared by selecting powder which is sieved by a 100-mesh sieve as raw materials, and finally the prepared additive is sieved by a 50-mesh sieve, and the preparation method of the additive comprises the following steps: adding composite straw powder, soda, coal and water into a reaction container, then adding yeast, controlling the temperature of the reaction container to be 25-35 ℃, stirring while reacting, pouring the mixture into a reaction kettle after reacting for 6-7 hours, controlling the rotating speed to be 450-650 r/min, controlling the temperature to be 70-80 ℃, adding the mixture into a heating box after reacting for 5-15 minutes, heating for 15-25 minutes at 220-280 ℃, and finally grinding to prepare an additive, wherein the ratio of sulfur, argil, biological protein zinc and high-salinity hard water in the auxiliary agent is 2.5:1.3:0.2:6, the sulfur and the argil are powder materials with 20-50 meshes, and the preparation method of the auxiliary agent comprises the following steps: firstly adding argil into high-salinity hard water, stirring for 15-25 minutes at the rotating speed of 250-350 r/min, then adding sulfur and biological protein zinc, increasing the rotating speed to 450-650 r/min, increasing the temperature to 45-60 ℃, continuing to stir for 25-35 minutes, then drying and dehydrating to obtain particles, adding the particles into an oil bath kettle at 145-160 ℃ for heating, heating for 15-25 minutes, then immediately pouring the mixture into a container at 45 ℃ below zero for half an hour for cooling, taking out the mixture after cooling, and finally preparing the auxiliary agent.

The preparation method of the multifunctional viscosity reducing agent comprises the following steps:

s1: adding nonylphenol polyoxyethylene ether and the modified mixture into a reaction kettle, raising the temperature of the reaction kettle to 55-65 ℃, controlling the rotating speed to be 250-350 r/min, and reacting for 5-15 minutes;

s2: adding azacarbene iron and biological enzyme, raising the temperature to 25-35 ℃, reacting for 5-10 minutes, adding water into the mixture, continuing to react for 15-25 minutes, and stopping heating to obtain a first solution;

s3: adding ethanol, an additive and an auxiliary agent into stirring equipment, keeping the interior of the stirring equipment in a vacuum state, raising the temperature to 65-75 ℃, and uniformly stirring to obtain a second solution;

s4: adding the second solution into the refrigerating chamber, cooling the second solution to minus 25 ℃, adding the second solution into the first solution, and rapidly stirring the solution to prepare a mixed solution;

s5: and adding the mixed solution into drying equipment for drying and dehydrating to finally prepare the multifunctional viscosity reducer.

Referring to FIG. 1, example V

The embodiment provides a multifunctional viscosity reducer, which comprises the following components in parts by mass: 20 parts of water, 16 parts of biological enzyme, 6 parts of nonylphenol polyoxyethylene ether, 6 parts of azacarbene iron, 6 parts of ethanol, 2 parts of modified mixture, 2 parts of additive and 2 parts of auxiliary agent, wherein the modified mixture comprises modified soda ash and floating soil of saline-alkali soil, the additive comprises composite straw powder, soda and coal, the auxiliary agent comprises sulfur, argil, zinc bioprotein and high-salinity hard water, and the modification method of the soda ash comprises the following steps: mixing soda ash, ammonium nitrate and biological enzyme according to the proportion of 7:1:2, then adding the mixture into a reaction kettle, extracting air in the reaction kettle, controlling the temperature in the reaction kettle to be 125-135 ℃, reacting for 25-30 minutes, then injecting mixed gas into the reaction kettle, wherein the mixed gas comprises 50% of helium, 30% of neon and 20% of argon, reducing the temperature to 85-95 ℃, reacting for 35-45 minutes, then discharging the residual mixed gas, injecting air after the temperature in the reaction kettle is reduced to 45-60 ℃, naturally cooling to normal temperature, then pouring the mixture into grinding equipment for grinding until the powder passes through a 100-mesh sieve, and preparing the modified soda ash, and the modification method of the floating soil of the saline-alkali soil comprises the following steps: adding 85% of saline-alkali soil float, 10% of tributyl citrate and 5% of tungstate into high-salinity hard water, then adding the mixed solution into a reaction kettle, controlling the rotation speed of the reaction kettle to be 220-320 r/min, raising the temperature to 65-80 ℃, reacting for 25-35 minutes, then adding the solution into a dehydration container for heating, removing water in the mixture, drying, then placing the mixture into a baking device for baking at 125-145 ℃, baking for 15-25 minutes in an oxygen-free environment, finally grinding to obtain the modified saline-alkali soil float, preparing the soda and the saline-alkali soil float according to the ratio of 40-60% to 40-60% in the modified mixture, storing the mixed modified mixture in a container at the temperature of 45-60 ℃, controlling the ratio of the composite straw powder, the soda and the coal in the additive to be 6.5:1.5:2, the composite straw powder consists of wheat straw powder, rice straw powder, wheat bran powder, rice hull powder, peanut hull powder and corn straw powder, the composite straw powder is prepared by selecting powder which is sieved by a 50-mesh sieve as raw materials, the soda and coal are prepared by selecting powder which is sieved by a 100-mesh sieve as raw materials, and finally the prepared additive is sieved by a 50-mesh sieve, and the preparation method of the additive comprises the following steps: adding composite straw powder, soda, coal and water into a reaction container, then adding yeast, controlling the temperature of the reaction container to be 25-35 ℃, stirring while reacting, pouring the mixture into a reaction kettle after reacting for 6-7 hours, controlling the rotating speed to be 450-650 r/min, controlling the temperature to be 70-80 ℃, adding the mixture into a heating box after reacting for 5-15 minutes, heating for 15-25 minutes at 220-280 ℃, and finally grinding to prepare an additive, wherein the ratio of sulfur, argil, biological protein zinc and high-salinity hard water in the auxiliary agent is 2.5:1.3:0.2:6, the sulfur and the argil are powder materials with 20-50 meshes, and the preparation method of the auxiliary agent comprises the following steps: firstly adding argil into high-salinity hard water, stirring for 15-25 minutes at the rotating speed of 250-350 r/min, then adding sulfur and biological protein zinc, increasing the rotating speed to 450-650 r/min, increasing the temperature to 45-60 ℃, continuing to stir for 25-35 minutes, then drying and dehydrating to obtain particles, adding the particles into an oil bath kettle at 145-160 ℃ for heating, heating for 15-25 minutes, then immediately pouring the mixture into a container at 45 ℃ below zero for half an hour for cooling, taking out the mixture after cooling, and finally preparing the auxiliary agent.

The preparation method of the multifunctional viscosity reducing agent comprises the following steps:

s1: adding nonylphenol polyoxyethylene ether and the modified mixture into a reaction kettle, raising the temperature of the reaction kettle to 55-65 ℃, controlling the rotating speed to be 250-350 r/min, and reacting for 5-15 minutes;

s2: adding azacarbene iron and biological enzyme, raising the temperature to 25-35 ℃, reacting for 5-10 minutes, adding water into the mixture, continuing to react for 15-25 minutes, and stopping heating to obtain a first solution;

s3: adding ethanol, an additive and an auxiliary agent into stirring equipment, keeping the interior of the stirring equipment in a vacuum state, raising the temperature to 65-75 ℃, and uniformly stirring to obtain a second solution;

s4: adding the second solution into the refrigerating chamber, cooling the second solution to minus 25 ℃, adding the second solution into the first solution, and rapidly stirring the solution to prepare a mixed solution;

s5: and adding the mixed solution into drying equipment for drying and dehydrating to finally prepare the multifunctional viscosity reducer.

Comparing the conventional viscosity reducing agent with the viscosity reducing agents prepared in examples one to five, the viscosity reducing agents prepared in examples one to five are as follows:

as can be seen from the above table, the viscosity reducing rate at high temperature and the cracking of heavy components of the viscosity reducing agent prepared by the present invention are significantly improved, and two are the best examples.

The above description is only for the preferred embodiment of the present invention, but the scope of the present invention is not limited thereto, and any person skilled in the art should be considered to be within the technical scope of the present invention, and the technical solutions and the inventive concepts thereof according to the present invention should be equivalent or changed within the scope of the present invention.