CN114702087A - Treating agent for removing heavy metals in aquatic product waste and application thereof - Google Patents

Treating agent for removing heavy metals in aquatic product waste and application thereof Download PDF

Info

Publication number
CN114702087A
CN114702087A CN202210627159.0A CN202210627159A CN114702087A CN 114702087 A CN114702087 A CN 114702087A CN 202210627159 A CN202210627159 A CN 202210627159A CN 114702087 A CN114702087 A CN 114702087A
Authority
CN
China
Prior art keywords
aquatic product
parts
heavy metals
agent
treating agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN202210627159.0A
Other languages
Chinese (zh)
Inventor
焦永康
刘双虎
赵龙梅
范占权
李华帅
高硕�
邢振平
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hebei Xietong Environmental Protection Technology Co ltd
Original Assignee
Hebei Xietong Environmental Protection Technology Co ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hebei Xietong Environmental Protection Technology Co ltd filed Critical Hebei Xietong Environmental Protection Technology Co ltd
Priority to CN202210627159.0A priority Critical patent/CN114702087A/en
Publication of CN114702087A publication Critical patent/CN114702087A/en
Pending legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00Treatment of water, waste water, or sewage
    • C02F1/66Treatment of water, waste water, or sewage by neutralisation; pH adjustment
    • CCHEMISTRY; METALLURGY
    • C02TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02FTREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2101/00Nature of the contaminant
    • C02F2101/10Inorganic compounds
    • C02F2101/20Heavy metals or heavy metal compounds
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/80Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
    • Y02A40/81Aquaculture, e.g. of fish

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Hydrology & Water Resources (AREA)
  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Water Supply & Treatment (AREA)
  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Fertilizers (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

The invention relates to a treating agent for removing heavy metals in aquatic product wastes, which comprises the following components, by weight, 30-70 parts of chelate, 1-5 parts of pH regulator, 0.1-1.0 part of thickener, 2-15 parts of dispersant, 1-10 parts of emulsifier and 100 parts of water. The invention also provides application of the treating agent, wherein the treating agent is applied to aquatic product wastes, and the using amount of the treating agent is 25kg-200 kg/ton. The treatment agent can effectively remove the heavy metal and salt contents in aquatic product wastes; meanwhile, the blockage of organic fertilizer fermentation caused by the existence of heavy metals can be avoided, and when the method is applied to aquatic product waste to remove heavy metals, high-quality liquid organic fertilizer can be produced more effectively.

Description

Treating agent for removing heavy metals in aquatic product waste and application thereof
Technical Field
The invention belongs to the technical field of aquatic product waste treatment, and particularly relates to a treating agent for removing heavy metals in aquatic product waste and application thereof.
Background
Along with the development of social economy in recent years, industrial and agricultural wastewater and domestic sewage are discharged in large quantities, so that the whole water environment is damaged to a certain extent; in addition, improper exploitation and utilization of mineral resources and rainwater washing cause a large amount of heavy metals to be lost along with water and soil, and further aggravate heavy metal pollution to fresh water and even ocean water environment. Most of the phytophagous fishes feed on phytoplankton or organic matters in water and bottom sediment, heavy metals in the phytophagous fishes can be accumulated in different tissues and organs of the phytophagous fishes through the action of biological enrichment, and the fishes can further enrich the heavy metals in the bodies of the fishes through the modes of respiration of gills, permeation of skins, ingestion of the aquatic animals and plants polluted by the heavy metals and the like, so that the negative influence on the growth and development of the fishes is generated, and certain potential safety hazards also exist for consumers. This phenomenon is also more pronounced with the food chain, and therefore the content of heavy metal species at the top of the food chain is higher.
Along with the urbanization, more and more fishery clusters appear, so that the concentrated slaughtering of aquatic products is caused; with the help of nutriologists, fishery processing factories have the ability to select edible parts, so that the risk of eating heavy metals by people is avoided to a greater extent; however, how to treat the waste becomes a more troublesome problem for the processing plant. There are generally two approaches to the disposal of these wastes: the feed is used for breeding other animals; secondly, the treated fertilizer is used as a fertilizer in agricultural production. The treatment of heavy metals in the waste cannot be exceeded by the two aspects, and if the treatment is improper, the risk is caused to the health of human beings.
In the prior art, the chinese patent with application number 201410002729.2 discloses a method for degrading heavy metals in the process of temporarily rearing aquatic animals, which is to add compound fish vitamins, or EDTA, or a mixture of compound fish vitamins and EDTA into the feed during temporarily rearing aquatic animals; the addition amount of the compound vitamin in the feed is 4-10 g/Kg; the addition amount of EDTA is 1.0-3.2 g/Kg.
The Chinese patent with the application number of 201910945380.9 discloses a harmless treatment method for strengthening heavy metal removal of aquaculture tail water, which comprises the following steps: 1) arranging a planting pot on the floating bed, wherein the planting pot is provided with an interlayer, the interlayer is filled with a permeable protective layer, and the side wall of the planting pot is provided with permeable holes; 2) mixing the modified mineral adsorbent with soil to prepare composite soil; 3) planting the water cress seedlings in the planting pots by using composite soil; 4) putting the floating bed into a culture pond; 5) pulling out the grown mature cress with roots, planting new cress seedlings in a planting pot, and ridging by using composite soil; 6) repeating the step 4) and the step 5). The modified mineral adsorbent adsorbs heavy metal ions in the aquaculture water, and the rhizome of the cress adsorbs the heavy metal ions in the composite soil, so that the heavy metal ions in the aquaculture tail water can be timely treated.
In order to ensure food safety and realize green environmental protection, the aquatic product waste heavy metal treatment agent which is simple and convenient and has strong degradation capability needs to be developed.
Disclosure of Invention
In order to overcome the defects of the prior art, the invention provides a treating agent for removing heavy metals in aquatic product wastes and application thereof, and the treating agent can reduce the residues of heavy metals in fishery aquatic product wastes and subsequent organic fertilizers.
The technical scheme adopted by the invention is as follows: a treating agent for removing heavy metals in aquatic product wastes comprises, by weight, 30-70 parts of chelate, 0.5-5 parts of pH regulator, 0.1-1.0 part of thickener, 2-15 parts of dispersant, 1-10 parts of emulsifier and 100 parts of water.
The environment-friendly water-based paint further comprises the following components, by weight, 60 parts of chelate, 3 parts of pH regulator, 0.5 part of thickener, 10 parts of dispersant, 5 parts of emulsifier and 21.5 parts of water.
Further, the chelate is one of iminodisuccinic acid, iminodisuccinic acid sodium, iminodisuccinic acid potassium and iminodisuccinic acid ammonium, and the mass fraction of the chelate is 40% aqueous solution; the pH regulator is sulfuric acid, hydrochloric acid, sodium hydroxide, potassium hydroxide or ammonia water, and can be selected from commercially available common solution; the thickening agent is gelatin, gum arabic, xanthan gum or polyvinyl alcohol; the dispersant is sodium lignosulfonate or calcium lignosulfonate.
Further, the emulsifier is one of a surfactant op and a surfactant NP.
Further, the emulsifier is a surfactant op-10 or NP-12.
Further, the preparation method comprises the following steps,
s1, weighing the chelate, the pH regulator, the thickening agent, the dispersing agent, the emulsifier and water according to a preset proportion;
s2, mixing and stirring the chelate, the thickening agent, the dispersing agent, the emulsifying agent and the water uniformly, and then adjusting the pH value of the mixed solution to 4.5-8.5 by using a pH regulator.
Further, in step S2, the stirring rate is 50-100 r/min.
The invention also provides application of the treating agent, and the treating agent is mixed with the aquatic product waste to degrade heavy metals in the aquatic product waste.
Furthermore, the treating agent is applied to heavy metal degradation of aquatic product waste with the heavy metal content of not more than 1600mg/kg, and the using amount is 25kg-200 kg/ton.
Further, the treatment process of heavy metal degradation comprises the following steps of firstly, mixing aquatic product waste with water, and grinding the aquatic product waste into particles with the particle size of 20 microns, wherein the adding amount of the water is 30-40% of the mass of the aquatic product waste;
step two, mixing the mixture obtained in the step one with a treating agent and grinding the mixture to 5 microns;
step three, stirring the mixture obtained in the step two for 1 to 3 hours at a speed of between 50 and 200 r/min;
step four, filtering and separating the mixture obtained in the step three by using a microporous filter membrane with the filtering pore diameter of 0.5-1.5 mu m.
The invention has the beneficial effects that:
the treatment agent can effectively remove the heavy metal and salt contents in fishery aquatic waste; meanwhile, the blockage of organic fertilizer fermentation caused by the existence of heavy metals can be avoided, and when the method is applied to removing the heavy metals from fishery aquatic waste, the high-quality organic fertilizer can be more effectively produced.
Drawings
FIG. 1 is a graph showing the compositional content of the treating agent of example 1 of the present invention;
FIG. 2 is a graph showing the compositional content of the treating agent of example 2 of the present invention;
FIG. 3 is a graph showing the compositional content of the treating agent of example 3 of the present invention;
FIG. 4 is a schematic flow diagram of the application of the treating agent of the present invention.
Detailed Description
To further illustrate the technical means and effects of the present invention adopted to achieve the predetermined objects, the following detailed description of the embodiments, structures, features and effects according to the present invention will be made with reference to the accompanying drawings and preferred embodiments.
Example 1
The invention provides a treating agent for removing heavy metals in aquatic product waste, which mainly comprises a main material chelating agent selected from iminodisuccinic acid, iminodisuccinic acid sodium and iminodisuccinic acid potassium, and a pH regulator, a dispersing agent, a thickening agent and an emulsifying agent are added at the same time; after being crushed by a wet method, the fishery aquatic product waste is mixed with the composition to extract heavy metals and then is physically separated, so that heavy metal chelate is separated from the waste, and the effect of reducing the heavy metals is achieved; is more beneficial to the production of high-quality organic fertilizer.
The pH regulator mainly acts to promote the activity of heavy metals.
The dispersing agent mainly plays a role in promoting the suspension of materials and increasing the extraction efficiency.
The emulsifier mainly has the functions of reducing surface activity and improving extraction efficiency.
As shown in figures 1 and 4, the composition comprises, by weight, 60 parts of chelate imino disuccinic acid potassium, 3 parts of pH regulator industrial hydrochloric acid, 0.5 part of thickener gelatin, 10 parts of dispersant sodium lignosulfonate, 105 parts of emulsifier op-105 and 21.5 parts of water.
The effective content of the chelate imino disuccinic acid potassium is 40 percent, and the balance is water.
In the preparation of the treating agent, water, chelate imino disuccinic acid potassium, a thickener gelatin, a dispersant sodium lignosulfonate and an emulsifier op-10 are respectively added into a liquid mixing device in proportion, a mixed solution is formed after the materials are dissolved and uniformly stirred, a pH regulator industrial hydrochloric acid is added into the mixed solution in proportion to regulate the pH of the mixed solution to 4.5-8.5, and the treating agent in the embodiment 1 is obtained after uniform stirring; the stirring speed is controlled in the whole process to avoid generating a large amount of bubbles, preferably 50-100r/min, in this embodiment 80 r/min.
The heavy metals in the aquatic product waste are degraded after the treating agent is mixed with the aquatic product waste.
The treating agent is mainly used for removing and separating heavy metals in fishery aquatic product waste, and the using amount is based on: the treating agent is applied to heavy metal degradation of aquatic product waste with the heavy metal content of less than or equal to 1600mg/kg, and the using amount is 25kg-200kg (treating agent) per ton (aquatic product waste). The method is used for degrading the heavy metals in the fishery aquatic product waste.
In the invention, the heavy metal degradation treatment process comprises the following steps of firstly, mixing aquatic product waste with water, and grinding the aquatic product waste and the water in a colloid mill to a particle size of 20 mu m, wherein the suspension is a primary waste suspension; the adding amount of water is 35% of the mass of the aquatic product waste;
step two, mixing the mixture primary waste suspension obtained in the step one with a treating agent, adding a proper amount of inert zirconium beads into a colloid mill, and continuously grinding to 5 microns, wherein the suspension is a secondary waste suspension;
in order to ensure the completeness of extraction, the following scheme is referred to the addition amount of the treating agent: generally, 25-200 kg/ton of treating agent is added, and the maximum treating concentration is 1600 mg/kg; the addition amount of the treating agent with the heavy metal content lower than 200mg/kg is 25 kg/ton, on the basis, 25 kg/ton of the treating agent is required for every 200mg/kg of heavy metal in the waste, and the like.
Step three, transferring the mixture secondary waste suspension obtained in the step two into a reaction kettle, and stirring and extracting for 2 hours at the speed of 100 r/min;
step four, filtering and separating the mixture obtained in the step three by using a microporous filter membrane with the filtering pore diameter of 0.5-1.5 mu m. The filter residue is used for preparing the organic fertilizer, and the specific preparation process refers to the conventional process of the organic water-soluble fertilizer; detecting the content of heavy metal in the filtrate, adding a silicate precipitator with the heavy metal content of 10-15 times into the filtrate for treatment, removing the heavy metal from the filtrate and treating the heavy metal, and recycling the residual filtrate for extraction and separation of the heavy metal in other batches.
The treating agent can effectively remove heavy metals in fishery aquatic waste, and the reduction of salt in the two processes of separation by using the treating agent is mainly carried out by dissolving salt in aqueous solution and filtering, so that the salt content can be reduced.
Example 2
As shown in figures 2 and 4, the composition comprises, by weight, 70 parts of chelate imino sodium disuccinate, 3 parts of pH regulator industrial sulfuric acid, 0.1 part of thickener xanthan gum, 2 parts of dispersant sodium lignosulfonate, 1210 parts of emulsifier NP-1210 parts and 14.9 parts of water.
The effective content of the chelate imino sodium disuccinate is 40 percent, and the balance is water.
In the preparation of the treating agent of the embodiment, water, chelate imino sodium disuccinate, a thickener xanthan gum, a dispersant sodium lignosulfonate and an emulsifier NP-12 are respectively added into a liquid mixing device according to a certain proportion, a mixed solution is formed after the materials are dissolved and uniformly stirred, a pH regulator industrial sulfuric acid is added according to a certain proportion to regulate the pH of the mixed solution to 4.5-8.5, and the treating agent of the embodiment 2 is obtained after uniform stirring; the stirring speed is controlled in the whole process to avoid generating a large amount of bubbles, preferably 50-100r/min, in this embodiment 50 r/min.
The heavy metals in the aquatic product waste are degraded after the treating agent is mixed with the aquatic product waste.
The treating agent is mainly used for removing and separating heavy metals in fishery aquatic product waste, and the using amount is based on: the treating agent is applied to heavy metal degradation of aquatic product waste with the heavy metal content of less than or equal to 1600mg/kg, and the using amount is 25kg-200kg (treating agent) per ton (aquatic product waste). The method is used for degrading the heavy metals in the fishery aquatic product waste.
In the invention, the heavy metal degradation treatment process comprises the following steps of firstly, mixing aquatic product waste with water, and grinding the aquatic product waste and the water in a colloid mill to a particle size of 20 mu m, wherein the suspension is a primary waste suspension; the adding amount of water is 30% of the mass of the aquatic product waste;
step two, mixing the mixture primary waste suspension obtained in the step one with a treating agent, adding a proper amount of inert zirconium beads into a colloid mill, and continuously grinding to 5 microns, wherein the suspension is a secondary waste suspension;
in order to ensure the completeness of extraction, the following scheme is referred to for the addition amount of the treating agent: generally, 25-200 kg/ton of treating agent is added, and the maximum treating concentration is 1600 mg/kg; the addition amount of the treating agent with the heavy metal content lower than 200mg/kg is 25 kg/ton, on the basis, 25 kg/ton of the treating agent is needed to be added when the heavy metal content in the waste is increased by 200mg/kg, and the like.
Step three, transferring the mixture secondary waste suspension obtained in the step two into a reaction kettle, and stirring and extracting for 3 hours at the speed of 50 r/min;
step four, filtering and separating the mixture obtained in the step three by using a microporous filter membrane with the filtering pore diameter of 0.5-1.5 mu m. The filter residue is used for preparing the organic fertilizer, and the specific preparation process refers to the conventional process of the organic water-soluble fertilizer; detecting the content of heavy metal in the filtrate, adding a silicate precipitator with the heavy metal content of 10-15 times into the filtrate for treatment, removing the heavy metal from the filtrate and treating the heavy metal, and recycling the residual filtrate for extraction and separation of the heavy metal in other batches.
Example 3
As shown in fig. 3 and 4, the composition comprises, by weight, 30 parts of chelate imino disuccinic acid ammonium, 0.5 part of pH adjuster industrial ammonia water, 1.0 part of thickener polyvinyl alcohol, 15 parts of dispersant calcium lignosulfonate, op-101 parts of emulsifier and 52.5 parts of water.
The effective content of the chelate imino disuccinic acid ammonium is 40 percent, and the balance is water.
In the preparation of the treating agent, water, chelated imino disuccinic acid ammonium, a thickening agent polyvinyl alcohol, a dispersant calcium lignosulfonate and an emulsifier op-10 are respectively added into a liquid mixing device in proportion, a mixed solution is formed after the materials are dissolved and uniformly stirred, a pH regulator industrial ammonia water is added in proportion to regulate the pH of the mixed solution to 4.5-8.5, and the treating agent in the embodiment 3 is obtained after uniform stirring; the stirring speed is controlled in the whole process to avoid generating a large amount of bubbles, preferably 50-100r/min, in this embodiment 100 r/min.
The heavy metals in the aquatic product waste are degraded after the treating agent is mixed with the aquatic product waste.
The treating agent is mainly used for removing and separating heavy metals in fishery aquatic product waste, and the using amount is based on: the treating agent is applied to heavy metal degradation of aquatic product waste with the heavy metal content of less than or equal to 1600mg/kg, and the using amount is 25kg-200kg (treating agent) per ton (aquatic product waste). The method is used for degrading the heavy metals in the fishery aquatic product waste.
In the invention, the heavy metal degradation treatment process comprises the following steps of firstly, mixing aquatic product waste with water, and grinding the aquatic product waste and the water in a colloid mill to a particle size of 20 mu m, wherein the suspension is a primary waste suspension; the adding amount of water is 40% of the mass of the aquatic product waste;
step two, mixing the mixture primary waste suspension obtained in the step one with a treating agent, adding a proper amount of inert zirconium beads into a colloid mill, and continuously grinding to 5 microns, wherein the suspension is a secondary waste suspension;
in order to ensure the completeness of extraction, the following scheme is referred to for the addition amount of the treating agent: generally, 25-200 kg/ton of treating agent is added, and the maximum treating concentration is 1600 mg/kg; the addition amount of the treating agent with the heavy metal content lower than 200mg/kg is 25 kg/ton, on the basis, 25 kg/ton of the treating agent is needed to be added when the heavy metal content in the waste is increased by 200mg/kg, and the like.
Step three, transferring the mixture secondary waste suspension obtained in the step two into a reaction kettle, and stirring and extracting for 1h at 200 r/min;
step four, filtering and separating the mixture obtained in the step three by using a microporous filter membrane with the filtering pore diameter of 0.5-1.5 mu m. The filter residue is used for preparing the organic fertilizer, and the specific preparation process refers to the conventional process of the organic water-soluble fertilizer; detecting the content of heavy metal in the filtrate, adding a silicate precipitator with the heavy metal content of 10-15 times into the filtrate for treatment, removing the heavy metal from the filtrate and treating the heavy metal, and recycling the residual filtrate for extraction and separation of the heavy metal in other batches.
Example 4
The difference between the embodiment and the embodiment 3 is that the embodiment comprises the following components by weight part, 60 parts of chelate imino disuccinic acid ammonium, 5 parts of pH regulator industrial ammonia water, 0.4 part of thickener Arabic gum, 8 parts of dispersant calcium lignosulphonate, 104 parts of emulsifier op-104 and 22.6 parts of water.
The effective content of the chelate imino disuccinic acid ammonium is 40 percent, and the balance is water.
Examples of the experiments
130 kg/ton of the treating agent in example 1 was uniformly added to the fish head suspension containing 1100mg/kg of heavy metal lead (Pb) and crushed by wet grinding, and after separation, the organic fertilizer was obtained by biological fermentation, and the heavy metal content of the organic fertilizer and the fish head suspension which was not treated with the treating agent was measured. According to the related regulations of NY/T1429-2010 amino acid-containing water-soluble fertilizer and NY/T525-2021 organic fertilizer, on the basis of meeting the other indexes of the product, the content of heavy metal is detected to find that: the residual quantity of heavy metal lead is 45.00mg/kg, the untreated lead is 499.00mg/kg, and the total weight metal content is required to be less than or equal to 220mg/kg and the lead content is required to be less than or equal to 50mg/kg in the national organic fertilizer standard.
The organic fertilizer and the fish head suspension liquid which is not treated by the treating agent are used as two organic fertilizers to be applied to tomatoes, and the organic fertilizers are selected from the upper town unprotected places (114 degrees and 86 degrees from east China) of the hilly stone village ligusticum urban hills according to the experimental arrangement,38 degrees in northern latitude 02') and the organic matter content in the selected plots is 14.72g/kg, the nitrate nitrogen is 10.36mg/kg, the quick-acting potassium is 186.27mg/kg, and the available phosphorus is 18.25 mg/kg; mixing the above two organic fertilizers at a ratio of 5kg/667m2The using amount of the tomato is uniformly applied to the soil for planting the tomato before the tomato blooms, the comprehensive statistical yield is obtained from the first harvest in the season, then the quality of the tomato is researched, and during data analysis, a SPSS22.0 data analysis system is used for single-factor variance analysis and a Dunckan method is used for difference significance test; the experiment was conducted by setting an experimental treatment group (organic fertilizer treated with 130kg/T heavy metal extractant), a control group (organic fertilizer not treated with heavy metal extractant), and a blank CK (no organic fertilizer applied), each treatment was repeated 4 times, each time 300m2The test was carried out in a random distribution to obtain the test results in the table.
TABLE 1 test effect of tomato using different organic fertilizers
Figure 889248DEST_PATH_IMAGE001
When the two organic fertilizers are applied to tomatoes, the yield of a control group is increased by 5.53 percent compared with that of a blank group, and the yield of a treatment group is increased by 17.42 percent; the tomato quality is obviously improved, mainly embodied as the increase of chromaticity, the increase of VC content, the improvement of solid matters and flavonoids and the like; meanwhile, the incidence of the plants is low in the whole growing season, but 1-2 times of bactericide is used in the untreated growing stage.
At present, the technical scheme of the invention has been subjected to pilot plant test, namely a small-scale experiment before large-scale mass production of products; after the pilot test is finished, the investigation for the use of the user is carried out in a small range, and the investigation result shows that the satisfaction degree of the user is higher; the preparation of products for formal production for industrialization (including intellectual property risk early warning research) has been set forth.
Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the invention as defined by the appended claims.

Claims (10)

1. The treating agent for removing the heavy metals in aquatic product wastes is characterized by comprising the following components, by weight, 30-70 parts of chelate, 0.5-5 parts of pH regulator, 0.1-1.0 part of thickener, 2-15 parts of dispersant, 1-10 parts of emulsifier and 100 parts of water.
2. The treatment agent for removing the heavy metals in the aquatic product waste according to claim 1, which comprises the following components, by weight, 60 parts of a chelate, 3 parts of a pH regulator, 0.5 part of a thickener, 10 parts of a dispersant, 5 parts of an emulsifier, and 21.5 parts of water.
3. The aquatic product waste heavy metal removal treatment agent as claimed in claim 1, wherein the chelate is one of iminodisuccinic acid, sodium iminodisuccinate, potassium iminodisuccinate and ammonium iminodisuccinate, and the mass fraction of the chelate is a 40% aqueous solution; the pH regulator is sulfuric acid, hydrochloric acid, sodium hydroxide, potassium hydroxide or ammonia water; the thickening agent is gelatin, gum arabic, xanthan gum or polyvinyl alcohol; the dispersant is sodium lignosulfonate or calcium lignosulfonate.
4. The aquatic product waste heavy metal removal treatment agent as claimed in claim 1, wherein the emulsifier is one of a surfactant op and a surfactant NP.
5. The aquatic product waste heavy metal removal treatment agent as claimed in claim 4, wherein the emulsifier is a surfactant op-10 or NP-12.
6. The treatment agent for removing the heavy metals in the aquatic product waste according to claim 1, wherein the preparation method comprises the following steps,
s1, weighing the chelate, the pH regulator, the thickening agent, the dispersing agent, the emulsifier and water according to a preset proportion;
s2, mixing and stirring the chelate, the thickening agent, the dispersing agent, the emulsifying agent and the water uniformly, and then adjusting the pH value of the mixed solution to 4.5-8.5 by using a pH regulator.
7. The treatment agent for removing the heavy metals from the aquatic product waste according to claim 6, wherein in the step S2, the stirring speed is 50-100 r/min.
8. The application of the treatment agent for removing heavy metals in aquatic product waste as claimed in any one of claims 1 to 7, wherein the treatment agent is mixed with the aquatic product waste to degrade heavy metals in the aquatic product waste.
9. The application of the treatment agent for removing the heavy metals in the aquatic product wastes according to claim 8 is characterized in that the treatment agent is applied to the heavy metal degradation of the aquatic product wastes with the heavy metal content of not more than 1600mg/kg, and the use amount is 25 kg/ton to 200 kg/ton.
10. The application of the treating agent for removing the heavy metals in the aquatic product wastes according to claim 8, wherein the treatment process for degrading the heavy metals comprises the following steps of firstly, mixing the aquatic product wastes with water, grinding the mixture to have a particle size of 20 microns, and adding water in an amount of 30-40% by mass of the aquatic product wastes;
step two, mixing the mixture obtained in the step one with a treating agent, and grinding the mixture to 5 microns;
step three, stirring the mixture obtained in the step two for 1 to 3 hours at a speed of between 50 and 200 r/min;
step four, filtering and separating the mixture obtained in the step three by using a microporous filter membrane with the filtering pore diameter of 0.5-1.5 mu m.
CN202210627159.0A 2022-06-06 2022-06-06 Treating agent for removing heavy metals in aquatic product waste and application thereof Pending CN114702087A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202210627159.0A CN114702087A (en) 2022-06-06 2022-06-06 Treating agent for removing heavy metals in aquatic product waste and application thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202210627159.0A CN114702087A (en) 2022-06-06 2022-06-06 Treating agent for removing heavy metals in aquatic product waste and application thereof

Publications (1)

Publication Number Publication Date
CN114702087A true CN114702087A (en) 2022-07-05

Family

ID=82177687

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202210627159.0A Pending CN114702087A (en) 2022-06-06 2022-06-06 Treating agent for removing heavy metals in aquatic product waste and application thereof

Country Status (1)

Country Link
CN (1) CN114702087A (en)

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004033374A1 (en) * 2002-10-08 2004-04-22 Kemira Oyj Method and medium for the removal of heavy metals from aqueous solutions
CN101947381A (en) * 2009-07-08 2011-01-19 东曹株式会社 The processing method of heavy metal treatment agent and heavy metal pollution material
CN104119923A (en) * 2013-04-25 2014-10-29 成都新朝阳作物科学有限公司 Heavy metal-polluted soil restoration agent and application thereof
CN107586003A (en) * 2017-08-22 2018-01-16 北京融达环科新材料科技有限公司 Sludge treating agent and method for sludge treatment
CN108821359A (en) * 2018-06-15 2018-11-16 颢葳环保科技南通有限公司 A kind of novel environment friendly stain remover
CN109627063A (en) * 2019-01-16 2019-04-16 吉林农业大学 A kind of method of animal husbandry rubbish production organic fertilizer
CN109809519A (en) * 2019-03-30 2019-05-28 刘华 A kind of Organic-inorganic composite sewage-treating agent and preparation method thereof

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2004033374A1 (en) * 2002-10-08 2004-04-22 Kemira Oyj Method and medium for the removal of heavy metals from aqueous solutions
CN101947381A (en) * 2009-07-08 2011-01-19 东曹株式会社 The processing method of heavy metal treatment agent and heavy metal pollution material
CN104119923A (en) * 2013-04-25 2014-10-29 成都新朝阳作物科学有限公司 Heavy metal-polluted soil restoration agent and application thereof
CN107586003A (en) * 2017-08-22 2018-01-16 北京融达环科新材料科技有限公司 Sludge treating agent and method for sludge treatment
CN108821359A (en) * 2018-06-15 2018-11-16 颢葳环保科技南通有限公司 A kind of novel environment friendly stain remover
CN109627063A (en) * 2019-01-16 2019-04-16 吉林农业大学 A kind of method of animal husbandry rubbish production organic fertilizer
CN109809519A (en) * 2019-03-30 2019-05-28 刘华 A kind of Organic-inorganic composite sewage-treating agent and preparation method thereof

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
方海兰: "《城市土壤生态功能与有机废弃物循环利用》", 31 January 2014, 上海科学技术出版社 *
陈斌等: "多齿配体-硅胶色谱介质的制备与评价", 《色谱》 *

Similar Documents

Publication Publication Date Title
CN107265659A (en) A kind of aquaculture microorganism substrate modifier with triple function and preparation method thereof
Rahman et al. Agricultural use of fishpond sediment for environmental amelioration
CN108083857A (en) A kind of method that feces of livestock and poultry biogas slurry integrated treatment prepares liquid organic fertilizer
CN112079519B (en) Emergency and long-acting control method for eutrophic water bloom
CN103027055A (en) Moss-algae killer and production method thereof
CN111115962B (en) Method for multi-combination treatment of industrial mariculture tail water
CN105478464A (en) Method for removing heavy metal in bottom mud
CN109231339A (en) A kind of water quality cleansing agent and preparation method thereof for aquaculture
CN106219705A (en) A kind of pure natural flocculant for changing at the bottom of aquaculture pond and preparation method thereof
CN105858777A (en) Garlic straw-nanocopper composite blue alga treatment agent and preparation method thereof
CN102674517A (en) Method for rapidly flocculating blue-green algae in water body
CN102765809B (en) Biological wetland forming growth promoter and preparation method thereof
CN114702087A (en) Treating agent for removing heavy metals in aquatic product waste and application thereof
CN108658388B (en) Method for improving transparency of eutrophic water body
CN106007275A (en) Freshwater aquaculture pond sediment conditioner
CN108925584A (en) A kind of preparation method of efficient algae removal agent
CN109395699A (en) A method of waste water is handled using microalgae and recycles phosphorus element
CN108178279A (en) A kind of method for treating water of carbon-based synergist concerted catalysis persulfate
CN107746224A (en) A kind of configuration of solid dephosphorization matrix and its processing method
CN106631462A (en) Method for producing liquid seaweed fertilizer by bamboo shoot wastewater
CN106748379A (en) A kind of method that bamboo shoots waste water produces Liquid Fertilizer
JP3362168B2 (en) Eutrophication prevention method
CN112661275A (en) Blue algae water purifying material for removing natural water eutrophication and eliminating biological compound mixing
KR101167968B1 (en) Manufacturing system of liquid manure using humic acid
CN104986930A (en) Biological agent for treating sludge on bottom of fish pond

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20220705

RJ01 Rejection of invention patent application after publication