CN114208433A - Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria - Google Patents

Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria Download PDF

Info

Publication number
CN114208433A
CN114208433A CN202111541558.7A CN202111541558A CN114208433A CN 114208433 A CN114208433 A CN 114208433A CN 202111541558 A CN202111541558 A CN 202111541558A CN 114208433 A CN114208433 A CN 114208433A
Authority
CN
China
Prior art keywords
steel
reaction tank
support
pipe
diameter
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.)
Granted
Application number
CN202111541558.7A
Other languages
Chinese (zh)
Other versions
CN114208433B (en
Inventor
臧淑英
谢桂林
吴祥文
解瑞峰
李苗
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.)
Harbin Normal University
Original Assignee
Harbin Normal University
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 Harbin Normal University filed Critical Harbin Normal University
Priority to CN202111541558.7A priority Critical patent/CN114208433B/en
Publication of CN114208433A publication Critical patent/CN114208433A/en
Application granted granted Critical
Publication of CN114208433B publication Critical patent/CN114208433B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Classifications

    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01B—SOIL WORKING IN AGRICULTURE OR FORESTRY; PARTS, DETAILS, OR ACCESSORIES OF AGRICULTURAL MACHINES OR IMPLEMENTS, IN GENERAL
    • A01B79/00—Methods for working soil
    • A01B79/02—Methods for working soil combined with other agricultural processing, e.g. fertilising, planting
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01B—SOIL WORKING IN AGRICULTURE OR FORESTRY; PARTS, DETAILS, OR ACCESSORIES OF AGRICULTURAL MACHINES OR IMPLEMENTS, IN GENERAL
    • A01B79/00—Methods for working soil
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01F—PROCESSING OF HARVESTED PRODUCE; HAY OR STRAW PRESSES; DEVICES FOR STORING AGRICULTURAL OR HORTICULTURAL PRODUCE
    • A01F29/00—Cutting apparatus specially adapted for cutting hay, straw or the like
    • A01F29/005—Cutting apparatus specially adapted for cutting hay, straw or the like for disintegrating and cutting up bales of hay, straw or fodder
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01F—PROCESSING OF HARVESTED PRODUCE; HAY OR STRAW PRESSES; DEVICES FOR STORING AGRICULTURAL OR HORTICULTURAL PRODUCE
    • A01F29/00—Cutting apparatus specially adapted for cutting hay, straw or the like
    • A01F29/09—Details
    • A01F29/10—Feeding devices
    • A—HUMAN NECESSITIES
    • A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01F—PROCESSING OF HARVESTED PRODUCE; HAY OR STRAW PRESSES; DEVICES FOR STORING AGRICULTURAL OR HORTICULTURAL PRODUCE
    • A01F29/00—Cutting apparatus specially adapted for cutting hay, straw or the like
    • A01F29/09—Details
    • A01F29/12—Discharge means
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F11/00—Other organic fertilisers
    • C—CHEMISTRY; METALLURGY
    • C05—FERTILISERS; MANUFACTURE THEREOF
    • C05F—ORGANIC FERTILISERS NOT COVERED BY SUBCLASSES C05B, C05C, e.g. FERTILISERS FROM WASTE OR REFUSE
    • C05F17/00—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation
    • C05F17/20—Preparation of fertilisers characterised by biological or biochemical treatment steps, e.g. composting or fermentation using specific microorganisms or substances, e.g. enzymes, for activating or stimulating the treatment
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/22—Improving land use; Improving water use or availability; Controlling erosion
    • Y—GENERAL 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
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/40—Bio-organic fraction processing; Production of fertilisers from the organic fraction of waste or refuse

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Environmental Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Soil Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Organic Chemistry (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Microbiology (AREA)
  • Molecular Biology (AREA)
  • Tropical Medicine & Parasitology (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，属于盐碱湿地生态修复技术领域，所用的有机质料加工设备由碎料机(1)、支撑钢架(2)、加液泵(3)、反应罐(4)、罐顶缓台(5)、合页封板(6)、加热管(7)、抽水泵(10)、总电源线(12)、总电源线插头(13)、导液槽(20)、搅拌电机(30)、接料冲斗(35)、传送带(40)、粉碎机(41)组成，其特征在于：所述的反应罐(4)是为秸秆碎和菌液生长提供适宜环境的罐体，内部设置有加热管(7)和搅拌棒(26)，搅拌电机(30)设置在反应罐(4)顶部中央，在底部设置一个差速器。该发明制作简单，可操作性强，成本低廉，效果明显。

Figure 202111541558

A method for rapidly replenishing the organic matter required in the restoration process of saline-alkali wetlands by utilizing high cellulolytic active bacteria belongs to the technical field of ecological restoration of saline-alkali wetlands. , dosing pump (3), reaction tank (4), tank top stage (5), hinge sealing plate (6), heating pipe (7), water pump (10), main power line (12), main Power cord plug (13), liquid guiding tank (20), stirring motor (30), material receiving bucket (35), conveyor belt (40), pulverizer (41), characterized in that: the reaction tank ( 4) It is a tank body that provides a suitable environment for the growth of broken straw and bacterial liquid, and is provided with a heating pipe (7) and a stirring rod (26) inside, and the stirring motor (30) is arranged at the top center of the reaction tank (4), and is arranged at the bottom. a differential. The invention has the advantages of simple manufacture, strong operability, low cost and obvious effect.

Figure 202111541558

Description

Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria
Technical Field
The invention relates to a method for rapidly supplementing organic matters required in a saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria, belonging to the technical field of saline-alkali wetland ecological restoration.
Background
At present, due to various reasons, salinization of all countries in the world is very serious, and the saline-alkali soil in China is more than 5 hundred million mu. Saline-alkali soil, called as "alkali Bara" by farmers, is a rough land where most plants cannot grow, and saline-alkali wetland is one of the saline-alkali soil. The saline-alkali soil is very poor, and the organic matter content is extremely low. The common saline-alkali soil improvement measures include the following measures: draining: for saline-alkali land blocks with low terrain, partial soil salinity can be taken away by draining ground water through digging drainage ditches; irrigating and washing salt: according to the law that salt comes with water and goes with water, water is filled into the ground to form a water layer with a certain depth on the ground, so that salt in the soil is fully dissolved, and the dissolved salt is discharged from a drainage ditch, so that the salt content of the soil is reduced; planting rice: planting rice in saline-alkali soil with sufficient water source is also an effective improvement measure, because a water layer is usually kept in a common field after the rice is planted, the water content of the soil is in a saturated state, and the salinity concentration in a paddy field is lower than that in a dry field under the condition of the same soil salinity, the salinity in the soil can be leached and discharged through long-time flooding and water drainage and water change; applying organic fertilizer: the organic fertilizer can increase humus of soil, is beneficial to formation of granular structure, improves the conditions of ventilation, water permeability and nutrient of saline-alkali soil, and can neutralize the alkalinity of the soil by the organic acid generated after decomposition, thereby having better planting green manure effect; deep ploughing and deep scarification: deep ploughing and deep loosening are carried out on the saline-alkali wetland, a plough layer is deepened, salt leaching can be accelerated, salt return is prevented, the soil moisture conservation and drought resistance capability is enhanced, and the nutrient condition of soil is improved. Deep ploughing should be careful not to turn dark alkali to the surface; alkaline pressing of the soil: the soil dressing is soil replacement, the soil dressing can improve the physical properties of saline-alkali soil, has the functions of inhibiting salt, leaching salt, pressing alkali and increasing soil fertility, and can reduce the salt content of the soil to the extent of not harming the growth of crops, in common words: the reason is that the sand is pressed into alkali and the seiko plate is adopted; and (4) reasonable planting: the crops planted in the saline-alkali land need to be properly arranged according to the adaptability of the crops to saline-alkali, drought and waterlogging due to land planting, and the potential of agricultural production increase is fully exerted. According to the saline-alkali land improvement measures, the saline-alkali wetland is ideally improved, so that the improved saline-alkali wetland can serve the production and living of people, organic matters can be rapidly supplemented for the saline-alkali wetland in a large quantity, once the content of the organic matters is increased, a large quantity of fungi in the saline-alkali wetland soil can be rapidly grown and propagated, and effective organic substances are provided for the growth of saline-alkali plants. It has been found that a small number of organisms can grow in saline and alkaline environments and that these organisms often have "halophilic enzymes" which often have salt tolerance, heat tolerance and tolerance to organic solvents. The soil organic matter is the core of soil quality, and maintains a plurality of factors related to the survival and development of the earth and human, such as soil fertility, grain safety, climate change and the like. Plant residues are the main initial source of soil organic matter and are stably existed after being transformed into the soil organic matter through a complex decomposition process under the mediation of soil microorganisms. However, to date, much research has focused on the effects of microorganisms on the breakdown and mineralization of organic matter, and little attention has been paid to the role of microbial metabolic processes in the formation of soil organic matter. More and more researches show that the biomass of living microorganisms cannot represent the total amount of organic matters accumulated in soil through the turnover of microorganisms; the microbial death residues have longer turnover time in soil, have great significance for long-term retention and accumulation of organic matters, and are indexes for representing better contribution of microbial source organic matters to soil organic matters. Simpson et al analyzed the chemical structures of the black-lime soil and corresponding vegetation by nuclear magnetic resonance and found that the contribution of microbial-derived chemical groups (proteins/peptides) in soil organic matter reaches over 50%. The utilization and transformation processes of the soil microorganisms on plant residues are closely related to the community characteristics, activity and physiological characteristics of the soil microorganisms. The process of utilizing and holding plant residues by soil microorganisms is generally divided into two stages: firstly, the microorganisms decompose the plant residues in contact with the microorganisms and assimilate a part of the low molecular weight compounds (such as carbohydrates, proteins, etc.) produced during the decomposition process to satisfy their own growth, in which the plant residues are converted into soil microbial biomass carbon; secondly, the microbial biomass carbon is converted into organic matter of microbial origin through further metabolism of the microbial biomass carbon. During such repeated growth-metabolism, the microorganisms continuously and thoroughly convert the plant residues into soil organic matters in the form of metabolites (such as extracellular enzymes, extracellular polymers and the like) or residues (such as chitin, peptidoglycan and the like). Therefore, how to rapidly supplement organic matters for the saline-alkali wetland in large quantity becomes a great problem to be solved urgently, the method utilizes organic matter material processing equipment arranged at the head of the saline-alkali wetland, the organic matter material processing equipment firstly crushes straws, then conveys the crushed straws into a reaction tank, the upper part of the reaction tank is large, the lower part of the reaction tank is provided with a crusher, larger straw blocks which are not completely decomposed can be cut into fragments to fall into a receiving hopper below the crusher, a water spray pipe is arranged at the front end of the receiving hopper, more and more straws in the receiving hopper are continuously washed away by the water spray pipe and are brought into the saline-alkali wetland along with the shearing, as the straw blocks are thoroughly decomposed in the reaction tank, more than 80 percent can be decomposed in 10 days and almost become organic matters, and after the decomposed organic matters are released from a liquid guide groove connected with the rear end of the receiving hopper, the method is necessary for rapidly supplementing the organic matters required in the saline-alkali wetland restoration process by utilizing the high cellulose decomposition active bacteria.
Disclosure of Invention
In order to overcome the problem of how to rapidly supplement organic matters for the saline-alkali wetland in large quantities, the invention provides a method for rapidly supplementing the organic matters required in the saline-alkali wetland restoration process by utilizing high-cellulose decomposition active bacteria, which utilizes organic material processing equipment arranged at the head of the saline-alkali wetland, wherein the organic material processing equipment firstly crushes straws and then conveys the crushed straws into a reaction tank, the upper part of the reaction tank is large and the lower part of the reaction tank is small, a crusher is arranged at the lower opening of the reaction tank, larger straw blocks which are not completely decomposed can be sheared into fragments to fall into a receiving hopper below the crusher, a water spray pipe is arranged at the front end of the receiving hopper, the straws in the receiving hopper are more and more along with the shearing, and are continuously washed away by the water spray pipe and brought into the saline-alkali wetland, and the straw blocks are thoroughly decomposed in the reaction tank, more than 80 percent of the decomposed organic matters can be decomposed in 10 days and almost all the decomposed organic matters are changed into the organic matters, so that the decomposed organic matters are released from the liquid guide groove connected with the rear end of the material receiving hopper and irrigated to the saline-alkali wetland along the ditch in the saline-alkali wetland, and the aim of quickly supplementing the saline-alkali wetland with the organic matters required in the saline-alkali wetland restoration process is fulfilled.
The technical scheme adopted by the invention for solving the technical problems is as follows:
the invention relates to a method for rapidly supplementing organic matters required in the process of saline-alkali wetland restoration by utilizing high cellulose decomposition active bacteria, which is characterized in that a plurality of movable organic material processing devices are arranged at the water position of the saline-alkali wetland, straws are firstly crushed in the organic material processing devices, then the crushed materials are conveyed into a reaction tank, reaction liquid is simultaneously added into the reaction tank, the reaction liquid consists of three components, namely water, the high cellulose decomposition active bacteria and a bacterial liquid mate capable of promoting the high cellulose decomposition active bacteria to exert activity, and the proportion of the three components is 95: 1: 4, wherein the bacteria with high cellulose decomposition activity are all bacteria, actinomycetes or fungi with cellulose decomposition activity, and the bacteria are single strains or mixed solution of multiple strains no matter which bacteria; the bacterial liquid mate capable of promoting the activity of the high cellulose decomposition active bacteria is urea, ammonia water or ammonium bicarbonate, and experiments prove that the nitrogen fertilizers can obviously promote the activity of the high cellulose decomposition active bacteria; heating and stirring the crushed straws when the crushed straws react in the reaction tank so as to promote the decomposition speed of the straws; organic matters formed after straw decomposition flow out of a liquid guide groove connected with the rear end of a material receiving flushing hopper into the saline-alkali wetland under the flushing of water sprayed by a water pump spray pipe, and are irrigated to each corner of the saline-alkali wetland along a water channel of the saline-alkali wetland, and straw blocks are thoroughly decomposed in a reaction tank and can be decomposed by more than 80 percent within 10 days to almost become the organic matters, so that the decomposed and decomposed organic matters are released from the liquid guide groove and irrigated to the saline-alkali wetland along the channel in the saline-alkali wetland, and the aim of quickly supplementing the saline-alkali wetland to be repaired with the organic matters required in the saline-alkali wetland repairing process is fulfilled; used organic material processing equipment comprises crushed aggregates machine 1, support steelframe 2, liquid feeding pump 3, retort 4, tank deck buffer 5, hinge shrouding 6, heating pipe 7, suction pump 10, total power cord 12, total power cord plug 13, cistern 20, stirring rod 26, agitator motor pivot 27, tank deck guardrail 29, agitator motor 30, shielding wall 31, connect material fill 35, conveyer belt 40, rubbing crusher 41, its characterized in that: the reaction tank 4 is a tank body which provides a suitable environment for straw crushing and bacterial liquid growth, the top of the reaction tank is provided with a tank top slow platform 5, a stirring motor 30, a baffle wall 31, a tank top feeding hole 33 and a tank top guardrail 29, the inside of the reaction tank is provided with a heating pipe 7 and a stirring rod 26, and the outer surface of the side wall of the reaction tank 4 at the central position of the extending part of the support frame slow platform 24 is provided with a climbing ladder 28; the tank top buffering table 5 is a part between the tank top feeding hole 33 and the periphery of the top of the reaction tank 4; the climbing ladder 28 is a ladder for people to climb to the reaction tank 4, is made of steel, two side arms are made of round steel tubes, the thickness of the wall of each round steel tube is 2-5 mm, the diameter of the excircle of the cross section of each round steel tube is 3-5 cm, the upper ends of the two side arms are welded on the side edges of the top wall of the reaction tank 4, the middle of each side arm is welded in a lookout buffer of the support frame buffer 24, the lower end of each side arm is free, a cross rod in the middle of each two side arms is a flat steel tube, the horizontal direction of each flat steel tube is 5-10 cm, and the vertical direction of each flat steel tube is 1-2 cm; the baffle wall 31 is a raised steel plate at the inner side of the tank top feed port 33, the lower edge of the baffle wall is welded on the top wall of the reaction tank 4 at the edge of the tank top feed port 33, the upper edge is free, the highest position is 50-100 cm away from the upper surface of the top wall of the reaction tank 4, and the thickness of the steel plate of the baffle wall 31 is 0.5-1 cm; two sides of the center of the hinge seal plate 6 are respectively provided with 1 rotating shaft, and the rotating shafts can extend into bearings welded on two side walls of a tank top feed port 33 on the top wall of the reaction tank 4, so that the rotating shafts can rotate in the bearings; the tank top feed inlet 33 is sealed by a turnable hinge seal plate 6; the reaction tank 4 is divided into an upper part and a lower part, the upper part of the reaction tank 4 is cylindrical, the diameter of the cylinder is 1-5 meters, and the height of the cylinder is 2-5 meters; the lower part of the reaction tank 4 is in an inverted frustum shape, the diameter of the upper end circle of the inverted frustum shape of the reaction tank 4 is 1-5 m, the diameter of the lower end circle of the inverted frustum shape of the reaction tank 4 is 0.5-3 m, the lower end of the reaction tank 4 is communicated with the material crushing machine 1, the central cavity of the upper part and the lower part in the reaction tank 4 is a reaction tank cavity 25, the reaction tank cavity 25 is integrated, and no partition plate is arranged in the middle; the wall of the reaction tank 4 is made of steel, and the thickness is 0.5-2 cm; the heating pipe 7 is a part for heating materials in the whole reaction tank cavity 25, and the temperature is controlled by a controller, wherein the temperature range is the proper growth temperature range of the high cellulose decomposition active bacteria, and the temperature range is 36.5-37.5 ℃; the heating pipe 7 is in a U shape with an upward opening, two side arms are fixed on the opposite positions of the inner surface of the wall of the reaction tank 4, the bottom of the heating pipe is positioned in a reaction tank cavity 25 at the intersection of the upper part and the lower part of the reaction tank 4, the outer wall of the heating pipe 7 is a copper pipe, the thickness of the wall of the copper pipe is 0.5-1 mm, a heating resistance wire is arranged in the pipe, and the larger the reaction tank 4 is, the higher the power of the heating resistance wire is; the resistance wires are connected by ceramic dividing blocks; the stirring rod 26 is made of steel and has a circular cross section, the diameter of the circular shape of the stirring rod 26 is 1-5 cm, the distance between the two ends of the stirring rod 26 and the inner surface of the tank body of the reaction tank 4 is 10-20 cm, and the stirring rod 26 is fixedly connected with the rotating shaft 27 of the stirring motor at the center; the stirring motor rotating shaft 27 is a steel shaft which can rotate under the drive of a stirring motor 30 rotor, the upper end of the stirring motor rotating shaft 27 extends to the center of a differential mechanism at the lower part of the stirring motor 30, the lower end of the stirring motor rotating shaft 27 is fixedly connected with the stirring rod 26, the stirring motor rotating shaft 27 is made of steel, the cross section of the stirring motor rotating shaft 27 is circular, and the diameter of the circle of the stirring motor rotating shaft 27 is 2-5 cm, and the length of the circle of the stirring motor rotating shaft 27 is 1-3 m; the stirring motor 30 is arranged in the center of the top of the reaction tank 4, a differential is arranged at the bottom, the stirring motor 30 is integrally cylindrical, and the diameter of the cylindrical cross section of the stirring motor 30 is 30-100 cm, and the height of the stirring motor 30 is 30-50 cm; the stirring motor power line 32 is a double-strand copper core power line, the cross section of the copper core is circular, the diameter of the copper core of the stirring motor power line 32 is 2-5 mm, one end of the stirring motor power line 32 is connected with the stirring motor 30, and the other end of the stirring motor power line 32 is connected with the main power line 12.
One end of the crusher 1 is provided with a motor, the middle part of the crusher is provided with a spiral stirring propelling cabin, the other end of the crusher is provided with a shear plate, and a cleaning knife 52 is arranged outside the shear plate; the motor of the material crushing machine 1 is integrally cylindrical, the diameter of the cross section of the motor cylinder of the material crushing machine 1 is 10-50 cm, the height of the cross section of the motor cylinder is 10-30 cm, a rotor of the motor is connected with a spiral shaft in a spiral stirring propelling cabin to form a whole, the rotation of the rotor of the motor can easily drive the spiral shaft to rotate along with the rotation of the motor, the motor is fixed on one side of the upper surface of the center of an H support 21, electric energy is supplied by a branch power line of a main power line 12 connected with the motor, the spiral stirring propelling cabin is fixed on the upper surface of the center of the H support 21, one end of the spiral stirring propelling cabin is welded with the motor, and the other end of the spiral stirring propelling cabin is fixed on the other side of the upper surface of the center of the H support 21; the shearing plate of the material crushing machine 1 is a double-layer circular plate made of manganese steel, the double-layer circular plate is respectively a cutting plate 45 and a movable plate 49, the thicknesses of the cutting plate 45 and the movable plate 49 are both 0.5-1 cm, the cutting plate 45 is arranged outside the cutting plate 49, the diameter of the cutting plate 45 is equal to the inner diameter of the spiral stirring propelling cabin, the diameter of the movable plate 49 is 1-2 mm smaller than the inner diameter of the spiral stirring propelling cabin, the periphery of the cutting plate 45 is fixed at the other end of the spiral stirring propelling cabin, which is opposite to the motor, the outer surface of the cutting plate 45 and the outer surface of the end of the spiral stirring propelling cabin are in the same plane, a cutting plate bearing 48 is arranged in the center of the cutting plate 45, a cavity in the center of the cutting plate bearing 48 is a cutting plate bearing cavity 47, and the cutting plate bearing cavity 47 is used for a rotating shaft 51 to penetrate through, so that the inner ring of the cutting plate bearing 48 is fixed with the rotating shaft 51; the inner end of the rotating shaft 51 is connected with a spiral shaft in the spiral stirring propelling cabin and is integrated, the rotating shaft 51 is made of manganese steel and is cylindrical, the diameter of the circular cross section of the cylinder is 2-10 cm, the outer end of the rotating shaft 51 is free, and the surface of the outer end is symmetrically connected with a pair of cleaning knives 52; the cleaning knife 52 is quadrangular, the cross section of the quadrangular prism is square, the side length of the square is 1-2 cm, the length of the cleaning knife 52 is 4-20 cm, and the distance between one side surface and the outer surface of the chopping board 45 is 0.5-1 mm; a plurality of circular chopping board release holes 46 are arranged on the central circle of the board surface where the outer edge of the chopping board bearing 48 and the periphery of the chopping board are located at equal intervals, the diameter of each chopping board release hole 46 is 0.5-1 cm, each chopping board release hole 46 is a straight round hole and is cylindrical, and the peripheries of the inner end and the outer end of each chopping board release hole 46 are provided with obvious sharp edges to form a double-layer circular board which can be sheared and fixed; the movable plate 49 is positioned at the inner side of the chopping board 45, is fixed on the rotating shaft 51 and can rotate along with the rotation of the rotating shaft 51, and a plurality of movable plate releasing holes 50 are arranged on the central circle of the board surface between the surface of the rotating shaft 51 and the periphery of the movable plate 49 at equal intervals; when the movable plate release hole 50 is opposite to the anvil release hole 46, the central axis of the movable plate release hole 50 is aligned with the central axis of the anvil release hole 46; the movable plate release hole 50 is in a shape of a circular truncated cone, the upper bottom of the circular truncated cone faces outwards and has the same size as the chopping board release hole 46, the lower bottom of the circular truncated cone faces inwards, and the diameter of a circle in which the circular truncated cone is located is 0.7-1.4 cm; the center of the spiral stirring propelling cabin is provided with a spiral shaft, the outside of the spiral stirring propelling cabin is provided with a cylindrical cabin wall, one end of the cabin wall is welded on the side wall of the motor, the other end of the cabin wall is free, an opening at the free end is provided with a chopping board 45 and then is blocked by the chopping board 45, the center of the top of the cabin wall is provided with a circular opening, the periphery of the opening is welded with the periphery of the lower opening of the reaction tank 4, and straw scraps and organic matter liquid in the reaction tank 4 can enter the spiral stirring propelling cabin from the opening; one end of a screw shaft of the spiral stirring propelling module is connected with a rotor of a motor of the material crushing machine 1, the other end of the screw shaft is connected with a rotating shaft 51, and the outer surface of the screw shaft is provided with a spiral ridge bulge; the spiral stirring propelling cabin is externally provided with a cylindrical cabin wall which is made of stainless steel or aluminum alloy and has the thickness of 1-5 cm, and the cross section of the inner cavity of the cylindrical cabin wall has the circular diameter of 8-40 cm and the height of 20-100 cm.
The supporting steel frame 2 is made of steel, can move under the dragging of tractors and other traction equipment, and is used for supporting the material crushing machine 1, the liquid adding pump 3, the reaction tank 4 and the water suction pump 10, the top one is connected with the conveying belt 40 through the conveying belt supporting rod 42, and the supporting steel frame 2 consists of a horizontal support 53, an inclined supporting steel frame 22, a supporting cylinder frame 9, a material receiving buffer hopper support 15, a support wheel 17, a support wheel support handle 18, a support wheel body 19, an H support 21, a supporting cylinder frame reinforcing ridge 23, a supporting cylinder frame buffer table 24, a climbing ladder 28, a tank top guardrail 29, a traction rod jack 43 and a traction rod 44; the horizontal support 53 is a frame support in the horizontal direction, the whole horizontal support 53 is rectangular, the length of the rectangle of the horizontal support 53 is 2-10 m, the width of the rectangle of the horizontal support is 1-5 m, the steel pipes used on four sides of the rectangle are the same, the thickness of the wall of each steel pipe is 5-10 mm, the cross section of the inner cavity of each steel pipe is rectangular, the length of the rectangle of the inner cavity of each steel pipe is 5-10 cm, the width of the rectangle of the inner cavity of each steel pipe is 4-6 cm, and the steel pipes on the four sides are connected into a whole at four corners of the rectangle through welding to form the horizontal support 53; the inclined strut steel frames 22 are supports for supporting and fixing the support cylinder frame 9, the number of the inclined strut steel frames is 4, the lower end of each inclined strut steel frame 22 is welded at one angle of the horizontal support 53, the upper end of each inclined strut steel frame is welded at the upper edge of the support cylinder frame 9, the cross section of each inclined strut steel frame 22 is an isosceles triangle, the bottom edge of the isosceles triangle is arranged at the inner side, the vertex angle of the isosceles triangle is arranged at the outer side, the waist of the isosceles triangle is arranged above the outer side edge of the steel pipe of the horizontal support 53, the length of the waist of the isosceles triangle is 5-20 cm, and the vertex angle of the isosceles triangle is welded above the angle of the horizontal support 53; the support frame 9 is an inverted frustum-shaped steel cylinder, the upper part of the inverted frustum-shaped lower half part of the reaction tank 4 is arranged in the support frame 9 and is fixed by the support frame 9, the diameter of the upper end circle of the support frame 9 is 1-5 m, the diameter of the lower end circle of the support frame 9 is 0.5-3 m, and the thickness of the wall of the support frame 9 is 0.5-1 cm; the support frame buffer 24 is a steel pipe support at the upper opening edge of the support frame 9, the support frame buffer 24 comprises two parts, namely a lookout buffer and a hoop buffer, the lookout buffer is a buffer extending out from the upper end of an inverted-frustum-shaped steel cylinder of the support frame 9, the lower parts of the two side walls of the lookout buffer are supported by steel plates welded on the outer surface of the support frame 9 through side walls, the two ends of the outer side wall of the lookout buffer are respectively welded with the upper end of the inclined strut steel frame 22, and a climbing ladder 28 penetrates through the center of the lookout buffer; the hoop buffering table is arranged on the periphery of the lower edge of the upper part of the reaction tank 4 and consists of steel pipes with the width of 10-20 cm and the upper and lower thickness of 5-10 cm, and the thickness of the steel pipe wall of the hoop buffering table is 0.5-1 cm; the support frame reinforcing rib 23 is a steel pipe welded on the outer surface of the support frame 9 and is arranged in the vertical direction, the upper end of the support frame reinforcing rib 23 is welded on the lower surface of the hoop buffering table of the support frame buffering table 24, the lower end of the support frame reinforcing rib 23 is welded on the steel pipe on the lower opening edge of the support frame 9, the cross section of the support frame reinforcing rib 23 is rectangular, the length of the rectangular support frame reinforcing rib 23 is 3-5 cm, the width of the rectangular support frame reinforcing rib is 2-3 cm, and the thickness of the steel pipe wall is 0.5-1 cm; the support wheel 17 comprises a support wheel support handle 18 and a support wheel body 19, the support wheel support handle 18 is a steel rod between the support wheel body 19 and the horizontal support 53, the length is 20-50 cm, the cross section of the support wheel support handle 18 is rectangular, and the rectangular length of the support wheel support handle 18 is 5-10 cm, and the width is 2-5 cm; the support wheel body 19 is a rotatable part of the support wheel 17, the center is a rotating shaft, a bearing is arranged outside the rotating shaft, a wheel hub is arranged outside the bearing, a tire is arranged outside the wheel hub, the tire is made of rubber and is divided into an inner tire and an outer tire, and air is filled into the inner tire; the H support 21 is a support which is H-shaped in the middle of the horizontal support 53 and is used for supporting the material crushing machine 1, the material receiving punching hopper 35 and the liquid guide groove 20, two ends of the left side arm and the right side arm of the H support 21 are welded on the front support and the rear support of the horizontal support 53, the left side arm and the right side arm are made of connecting steel pipes, the width of each connecting steel pipe is 10-20 cm, the upper surface of each connecting steel pipe is welded with the material crushing machine 1, and the lower edge of the outer surface of the right side arm of the H support 21 is welded with the material receiving punching hopper 35 and the upper edge of one side wall of the liquid guide groove 20; one end of the receiving hopper 35 is plugged by a steel plate, one half of the other end is plugged by a steel plate, the other half is communicated with the liquid guide groove 20, and the end of the receiving hopper 35 with the plug is provided with an opening of the pipette 16 and an opening of the spray pipe 14; the liquid guide groove 20 is a groove with a U-shaped cross section, the bottom wall and the side wall are both made of steel plates, and the thicknesses of the steel plates used by the material receiving hopper 35 and the wall of the liquid guide groove 20 are both 2-5 mm; the material receiving punching hopper support 15 is a steel pipe for supporting the material receiving punching hopper 35, one end of the steel pipe is welded on the inner surface of the right side arm of the horizontal support 53, the other end of the steel pipe is welded on the right side wall of the material receiving punching hopper 35, the inner cavity of the cross section of the steel pipe is rectangular, the length of the rectangle is 3-5 cm, the width of the rectangle is 2-4 cm, and the thickness of the wall of the steel pipe is 0.5-1 cm; the draw bar 44 is a solid steel bar with one end welded at the center of the outer surface of the left arm of the horizontal bracket 53 and the other end free, the cross section of the draw bar 44 is rectangular, the length of the rectangle is 5-10 cm, and the width of the rectangle is 4-6 cm; the draw bar jack 43 is a cylindrical hole and is arranged at the free end of the draw bar 44, the diameter of the round cross section of the cylinder of the draw bar jack 43 is 3-5 cm, and the height is 4-6 cm; the total power line 12 is a double-strand copper core power line, the cross section of the copper core is circular, and the diameter of the copper core of the total power line 12 is 3-8 mm; the main power cord plug 13 is a three-phase plug, and is provided at a free end of the main power cord 12.
The liquid adding pump 3 is a water pump which utilizes an electric water pump to pump water from the material receiving hopper 35 into the reaction tank 4 to provide water for decomposing straw, is supplied with electric energy by a main power line 12 and is arranged on a horizontal bracket 53, and the liquid adding pump 3 comprises a liquid adding pipe 8 and a liquid suction pipe 16; the liquid adding pipe 8 is a water pipe at the upper part of the liquid adding pump 3, one end of the liquid adding pipe is communicated with the pump body of the liquid adding pump 3, the other end of the liquid adding pipe is free, the opening is arranged at a tank top feed inlet 33 at the top of the reaction tank 4, the middle part of the liquid adding pipe is fixed on the outer surface of the upper part of the reaction tank 4 in the vertical direction through a fixing ring, the liquid adding pipe 8 is made of rubber, the wall thickness is 0.5-1 cm, a spiral steel wire is embedded in the wall, the cross section of the steel wire is circular, the diameter of the circle is 2-5 mm, and the pipe diameter of the inner cavity of the liquid adding pipe 8 is 5-10 cm; the pipette 16 is a pipeline for sucking water out of the receiving hopper 35 under the suction of the pump body of the liquid adding pump 3, the pipette 16 is made of rubber, the wall thickness is 0.5-1 cm, a spiral steel wire is embedded in the wall, the cross section of the steel wire is circular, the diameter of the circle is 2-5 mm, the diameter of an inner cavity of the pipette 16 is 5-10 cm, one end of the pipette 16 is communicated with the pump body of the liquid adding pump 3, the other end of the pipette 16 extends to the bottom of the receiving hopper 35, and the end, at the bottom of the receiving hopper 35, of the pipette 16 is provided with a faucet.
The water pump 10 is a water pump which utilizes an electric water pump to pump water from water sources such as ditches and the like into the material receiving hopper 35 to wash the reaction tank 4 and organic matter liquid and straw crushing water discharged from the crusher 1 at the lower part of the reaction tank 4, is supplied with electric energy by a main power line 12 and is arranged on a horizontal support 53, and the water pump 10 comprises a water suction pipe 11 and a water spray pipe 14; the spray pipe 14 is a water pipe at the upper part of the water pump 10, one end of the spray pipe is communicated with the pump body of the water pump 10, the other end of the spray pipe is free, the opening is arranged at the position of the blocking wall of the receiving hopper 35, the middle part of the spray pipe is transversely arranged between the horizontal bracket 53 and the receiving hopper 35, the spray pipe 14 is a steel pipe, the wall thickness is 0.5-1 cm, and the pipe diameter of an inner cavity is 5-10 cm; the water suction pipe 11 is a pipeline for sucking water from water sources such as ditches and the like into the material receiving hopper 35 under the suction of the pump body of the water suction pump 10, the water suction pipe 11 is made of rubber, the wall thickness is 0.5-1 cm, spiral steel wires are embedded in the wall of the water suction pipe 11, the cross section of each steel wire is circular, the diameter of each steel wire is 2-5 mm, the diameter of an inner cavity of the water suction pipe 11 is 5-10 cm, one end of the water suction pipe 11 is communicated with the pump body of the liquid feeding pump 3, the other end of the water suction pipe extends into the water sources such as the ditches and the like, and the water suction pipe 11 is provided with a faucet at the end in the water sources such as the ditches and the like.
The smashing machine 41 is internally provided with a smashing roller, the base part of the smashing machine 41 is cuboid, the cuboid at the base part of the smashing machine 41 is 2-4 meters in length, 1-1.5 meters in width and 0.5-1 meter in height, 4 rollers are arranged at the lower part of the cuboid at the base part of the smashing machine 41 so as to move the whole smashing machine 41, and the smashing roller smashes straws fed from the feeding hole 38 of the smashing machine under the driving of a motor by the smashing machine 41; the pulverizer 41 is also internally provided with an air blowing structure; the crusher feed port 38 is a square opening where various straws are stuffed into the crusher 41; the crusher discharging nozzle 37 is a flat tube structure on the upper part of the crusher 41 opposite to the crusher feeding port 38, the crusher discharging nozzle 37 has a large and rectangular base opening, the rectangular length is 1-1.5 m, the width is 10-30 cm, the crusher discharging nozzle 37 has a small and oval free end opening, the oval long diameter is 10-30 cm, the short diameter is 10-15 cm, and the crusher discharging nozzle 37 has an opening positioned on the conveyor belt 40.
The conveying belt 40 consists of a conveying belt discharging barrel 34, a conveying belt surrounding barrel 36, a conveying belt receiving platform 39 and a conveying belt supporting rod 42, wherein the conveying belt discharging barrel 34 is a bent barrel at the top of the conveying belt 40, and the barrel wall of the conveying belt discharging barrel 34 is made of steel and is 1-5 mm thick; the base part of the conveyor belt discharging cylinder 34 is communicated with the conveyor belt surrounding cylinder 36, the end part is free, and the opening is arranged above the tank top feeding hole 33; the conveying belt surrounding cylinder 36 is positioned between the conveying belt discharging cylinder 34 and the conveying belt receiving platform 39 and is cylindrical, the diameter of the cylinder is 30-50 cm, the wall of the conveying belt surrounding cylinder 36 is made of steel, the thickness of the wall is 1-5 mm, and a belt capable of rotating back and forth is arranged in the conveying belt surrounding cylinder 36; the driving belt supporting rod 42 is made of steel and has a circular cross section, and the diameter of the driving belt supporting rod 42 is 3-10 cm, and the height of the driving belt supporting rod is 0.3-0.5 m; the conveyor belt receiving platform 39 is arranged horizontally, 4 rollers are arranged at the lower part of the conveyor belt receiving platform 39, and a horizontal belt is arranged at the upper part of the conveyor belt receiving platform 39.
The method for quickly supplementing organic matters required in the saline-alkali wetland restoration process by using the high-cellulose decomposition active bacteria has the advantages that the method for quickly supplementing the organic matters required in the saline-alkali wetland restoration process by using the high-cellulose decomposition active bacteria utilizes organic matter processing equipment arranged at the head of the saline-alkali wetland, the organic matter processing equipment firstly crushes straws and then conveys the crushed straws into a reaction tank, the reaction tank is large at the upper part and small at the lower part, a crushing machine is arranged at the lower opening, larger straw blocks which are not completely decomposed can be sheared into fragments to fall into a material receiving flushing hopper below the crushing machine, a water spray pipe is arranged at the front end of the material receiving flushing hopper, more and more straws are continuously flushed away into the saline-alkali wetland along with the shearing, and the straw blocks can be decomposed more than 80 percent in 10 days because the straw blocks are thoroughly decomposed in the reaction tank, almost all become organic matters, so after the decomposed and decomposed organic matters are released from the liquid guide groove connected with the rear end of the material receiving flushing hopper, the organic matters are irrigated to the saline-alkali wetland along the ditch in the saline-alkali wetland, and the aim of quickly supplementing the saline-alkali wetland with the organic matters required in the saline-alkali wetland restoration process is fulfilled. The method for rapidly supplementing organic matters required in the saline-alkali wetland restoration process by using the high-cellulose decomposition active bacteria has the advantages of simple process flow, strong operability, low cost and obvious effect.
Drawings
The invention is further described below with reference to the accompanying drawings.
FIG. 1 is a schematic view of the overall structure of organic material processing equipment of the method for rapidly supplementing organic matters required in the saline-alkali wetland restoration process by using high cellulose decomposition active bacteria.
FIG. 2 is a schematic view of the whole structure of a chopping block of a crusher of organic material processing equipment, which is a method for rapidly supplementing organic matters required in the saline-alkali wetland restoration process by using high cellulose decomposition active bacteria.
Fig. 3 is a schematic view of the overall structure of a movable plate of a crusher of organic material processing equipment, which is the method for rapidly supplementing organic matters required in the saline-alkali wetland restoration process by using high cellulose decomposition active bacteria.
In the figure, 1, a crusher, 2, a supporting steel frame, 3, a liquid adding pump, 4, a reaction tank, 5, a tank top buffer table, 6, a hinge seal plate, 7, a heating pipe, 8, a liquid adding pipe, 9, a support barrel frame, 10, a water suction pump, 11, a water suction pipe, 12, a general power line, 13, a general power line plug, 14, a water spray pipe, 15, a material receiving buffer bucket support, 16, a liquid suction pipe, 17, a support wheel, 18, a support wheel support handle, 19, a support wheel body, 20, a liquid guide groove, 21, an H support, 22, an inclined support steel frame, 23, a support barrel frame reinforcing rib, 24, a support barrel frame buffer table, 25, a reaction tank cavity, 26, a stirring rod, 27, a stirring motor rotating shaft, 28, a climbing ladder, 29, a tank top guardrail, 30, a stirring motor, 31, a shielding wall, 32, a stirring motor power line, 33, a tank top feeding port, 34, a conveying belt discharging barrel, 35, 36, a conveying belt surrounding barrel, 37, a crusher discharging nozzle, 38. the feeding port of the crusher is 39, the conveyor receiving platform is 40, the conveyor is 41, the crusher is 42, the conveyor supporting rod is 43, the draw bar jack is 44, the draw bar is 45, the chopping block is 46, the chopping block release hole is 47, the chopping block bearing cavity is 48, the chopping block bearing is 49, the movable plate is 50, the movable plate release hole is 51, the rotating shaft is 52, the cleaning knife is 53, and the horizontal support is provided.
Detailed Description
The first embodiment is as follows:
as shown in the figure, the method for rapidly supplementing organic matters required by the saline-alkali wetland restoration process by using high cellulose decomposition active bacteria is characterized in that a plurality of movable organic material processing devices are arranged at the edges of water wells, water channels, rivers, water bubbles, lakes and the like of the saline-alkali wetland, straws are firstly crushed in the organic material processing devices, then the crushed materials are conveyed into a reaction tank, reaction liquid is simultaneously added into the reaction tank, the reaction liquid consists of three components, namely water, the high cellulose decomposition active bacteria and a bacterial liquid mate capable of promoting the high cellulose decomposition active bacteria to exert the activity, and the proportion of the three components is 95: 1: 4, wherein the bacteria with high cellulose decomposition activity are all bacteria, actinomycetes or fungi with cellulose decomposition activity, and the bacteria are single strains or mixed solution of multiple strains no matter which bacteria; the bacterial liquid mate capable of promoting the activity of the high cellulose decomposition active bacteria is urea, ammonia water or ammonium bicarbonate, and experiments prove that the nitrogen fertilizers can obviously promote the activity of the high cellulose decomposition active bacteria; heating and stirring the crushed straws when the crushed straws react in the reaction tank so as to promote the decomposition speed of the straws; organic matters formed after straw decomposition flow out of the liquid guide groove connected with the rear end of the material receiving flushing hopper into the saline-alkali wetland under the flushing of water sprayed by the water pump spray pipe, and are irrigated to each corner of the saline-alkali wetland along the water channel of the saline-alkali wetland, and as straw blocks are thoroughly decomposed in the reaction tank, more than 80 percent of the decomposed organic matters can be decomposed within 10 days and almost all the decomposed organic matters become organic matters, after the decomposed organic matters are released from the liquid guide groove, the decomposed organic matters are irrigated to the saline-alkali wetland along the ditch in the saline-alkali wetland, so that the aim of quickly supplementing the saline-alkali wetland with the organic matters required in the saline-alkali wetland restoration process for the saline-alkali wetland to be restored is fulfilled. The organic material processing equipment used in the method for rapidly supplementing organic matters required in the saline-alkali wetland restoration process by utilizing high-cellulose decomposition active bacteria comprises a crusher 1, a supporting steel frame 2, a liquid adding pump 3, a reaction tank 4, a tank top buffering platform 5, a hinge sealing plate 6, a heating pipe 7, a liquid adding pipe 8, a support frame 9, a water suction pump 10, a water suction pipe 11, a main power line 12, a main power line plug 13, a water spray pipe 14, a material receiving buffer hopper support 15, a pipette 16, a support wheel 17, a support wheel support handle 18, a support wheel body 19, a liquid guide groove 20, an H support 21, an inclined supporting steel frame 22, a support frame reinforcing rib 23, a support frame buffering platform 24, a reaction tank cavity 25, a stirring rod 26, a stirring motor rotating shaft 27, a climbing ladder 28, a tank top guardrail 29, a stirring motor 30, a shielding wall 31, a stirring motor power line 32, a tank top feeding hole 33, a conveying belt discharging cylinder 34, a material receiving buffer hopper 35, a conveying belt enclosing cylinder 36, The crusher comprises a crusher discharging nozzle 37, a crusher feeding hole 38, a conveyor receiving platform 39, a conveyor 40, a crusher 41, a conveyor supporting rod 42, a traction rod insertion hole 43, a traction rod 44, an anvil 45, an anvil releasing hole 46, an anvil bearing cavity 47, an anvil bearing 48, a movable plate 49, a movable plate releasing hole 50, a rotating shaft 51, a cleaning knife 52 and a horizontal support 53. The crushing machine 1 is a structure for conveying the straw crushed materials decomposed in the reaction tank 4 into the receiving hopper 35, the whole structure is similar to a commercially available meat grinder, one end of the crushing machine 1 is provided with a motor, the middle part of the crushing machine is provided with a spiral stirring propulsion cabin, the other end of the crushing machine is provided with a shear plate, and a cleaning knife 52 is arranged outside the shear plate; the motor of the material crushing machine 1 is integrally cylindrical, the diameter of the cross section of the motor cylinder of the material crushing machine 1 is 10-50 cm, the height of the cross section of the motor cylinder is 10-30 cm, a rotor of the motor is connected with a spiral shaft in a spiral stirring propelling cabin to form a whole, the rotation of the rotor of the motor can easily drive the spiral shaft to rotate along with the rotation of the motor, the motor is fixed on one side of the upper surface of the center of an H support 21, electric energy is supplied by a branch power line of a main power line 12 connected with the motor, the spiral stirring propelling cabin is fixed on the upper surface of the center of the H support 21, one end of the spiral stirring propelling cabin is welded with the motor, and the other end of the spiral stirring propelling cabin is fixed on the other side of the upper surface of the center of the H support 21; the shearing plate of the material crushing machine 1 is a double-layer circular plate made of manganese steel, the double-layer circular plate is respectively a cutting plate 45 and a movable plate 49, the thicknesses of the cutting plate 45 and the movable plate 49 are both 0.5-1 cm, the cutting plate 45 is arranged outside the cutting plate 49, the diameter of the cutting plate 45 is equal to the inner diameter of a spiral stirring propelling cabin, the diameter of the movable plate 49 is 1-2 mm smaller than the inner diameter of the spiral stirring propelling cabin, the periphery of the cutting plate 45 is fixed at the other end of the spiral stirring propelling cabin, which is opposite to a motor, the outer surface of the cutting plate 45 and the outer surface of the end of the spiral stirring propelling cabin are in the same plane, a cutting plate bearing 48 is arranged in the center of the cutting plate 45, a cavity in the center of the cutting plate bearing 48 is a cutting plate bearing cavity 47, and the cutting plate bearing cavity 47 is used for a rotating shaft 51 to penetrate through, so that the inner ring of the cutting plate bearing 48 is fixed with the rotating shaft 51 in the center of the cutting plate 45, thereby ensuring that the rotating shaft 51 can rotate by the cutting plate bearing 48; the inner end of the rotating shaft 51 is connected with a spiral shaft in the spiral stirring propelling cabin and is integrated with the spiral shaft in the spiral stirring propelling cabin, the rotating shaft 51 can rotate along with the rotation of the spiral shaft in the spiral stirring propelling cabin, the rotating shaft 51 is made of manganese steel and is cylindrical, the diameter of the circular cross section of the cylinder is 2-10 cm, the outer end of the rotating shaft 51 is free, and the surface of the outer end is symmetrically connected with a pair of cleaning knives 52; the cleaning knife 52 is quadrangular, the cross section of the quadrangular prism is square, the side length of the square is 1-2 cm, the length of the cleaning knife 52 is 4-20 cm, the distance between one side surface of the cleaning knife and the outer surface of the chopping board 45 is 0.5-1 mm, the cleaning knife can be scraped on the outer surface of the chopping board 45, and after the straw fragments are extruded, the straw fragments can be scraped and thrown into the material receiving flushing hopper 35, so that the scraped straw fragments are flushed into the saline-alkali wetland along with water; a plurality of circular chopping board release holes 46 are arranged on the central circle of the board surface where the outer edge of the chopping board bearing 48 and the periphery of the chopping board are located at equal intervals, the diameter of each chopping board release hole 46 is 0.5-1 cm, each chopping board release hole 46 is a straight round hole and is cylindrical, and the peripheries of the inner end and the outer end of each chopping board release hole 46 are provided with obvious sharp edges to form a double-layer circular board which can be sheared and fixed; the movable plate 49 is positioned at the inner side of the chopping board 45, is fixed on the rotating shaft 51 and can rotate along with the rotation of the rotating shaft 51, and a plurality of movable plate releasing holes 50 are arranged on the central circle of the board surface between the surface of the rotating shaft 51 and the periphery of the movable plate 49 at equal intervals; when the movable plate release hole 50 is opposite to the anvil release hole 46, the central axis of the movable plate release hole 50 is aligned with the central axis of the anvil release hole 46; the movable plate release hole 50 is in a circular truncated cone shape, the upper bottom of the circular truncated cone is outward and has the same size with the chopping board release hole 46, the lower bottom of the circular truncated cone is inward, the diameter of a circle in which the circular truncated cone is located is 0.7-1.4 cm, and the large opening of the circular truncated cone-shaped movable plate release hole 50 is inward and the small opening is outward, so that straw scraps and water containing organic matters, which are pressed out from the spiral stirring propulsion cabin, can be well flushed into the chopping board release hole 46, when the straw scraps pass through the movable plate release hole 50 and the chopping board release hole 46, because the central shaft of the movable plate release hole 50 and the central shaft of the chopping board release hole 46 are positioned on the same straight line, the movable plate release hole 50 and the follow-up plate 49 rotate rapidly, the hole edges at the adjacent positions of the movable plate release hole 50 and the chopping board release hole 46 mutually form a scissor shape, the straw scraps can be cut into sections, are easier to fall into the receiving punching hopper 35 and are smaller, and are more favorable for being flushed away. The center of the spiral stirring propelling cabin is provided with a spiral shaft, the outside of the spiral stirring propelling cabin is provided with a cylindrical cabin wall, one end of the cabin wall is welded on the side wall of the motor, the other end of the cabin wall is free, an opening at the free end is provided with a chopping board 45 and then is blocked by the chopping board 45, the center of the top of the cabin wall is provided with a circular opening, the periphery of the opening is welded with the periphery of the lower opening of the reaction tank 4, and straw scraps and organic matter liquid in the reaction tank 4 can enter the spiral stirring propelling cabin from the opening; one end of a screw shaft of the spiral stirring propelling module is connected with a rotor of a motor of the material crushing machine 1, the other end of the screw shaft is connected with a rotating shaft 51, and the outer surface of the screw shaft is provided with a spiral ridge bulge; the spiral stirring propelling cabin is externally provided with a cylindrical cabin wall which is made of stainless steel or aluminum alloy and has the thickness of 1-5 cm, and the cross section of the inner cavity of the cylindrical cabin wall has the circular diameter of 8-40 cm and the height of 20-100 cm; like this, the garrulous and organic matter liquid of straw in retort 4 gets into the spiral from the spiral and stirs the propulsion cabin from the spiral and stir the opening at propulsion cabin top, the motor rotor rotates, it rotates to drive the screw axis, when the spiral arris ridge arch on screw axis surface rotates, with garrulous and organic matter liquid of straw forward the shear plate direction promotion of crushed aggregates machine 1, at shear plate department, liquid is released away from the passageway that the chopping block release hole 50 and chopping block release hole 46 are constituteed, the garrulous in-process of flowing out along with liquid of straw in the liquid, still can be further sheared by the shear plate, under the assistance of clearance sword 52, thereby drop to the material receiving hopper 35 along with liquid. The supporting steel frame 2 is a main support of organic material processing equipment used in a method for quickly supplementing organic matters required in the saline-alkali wetland restoration process by utilizing high-cellulose decomposition active bacteria, is made of steel, can move under the dragging of tractors such as tractors and the like, and is used for supporting the material crushing machine 1, the liquid adding pump 3, the reaction tank 4 and the water suction pump 10, the top part I is connected with a conveyor belt 40 through a conveyor belt supporting rod 42, and the supporting steel frame 2 consists of a horizontal support 53, an inclined supporting steel frame 22, a support cylinder frame 9, a material receiving buffer bucket support 15, a support wheel 17, a support wheel support handle 18, a support wheel body 19, an H support 21, a support cylinder frame reinforcing ridge traction rod 23, a support cylinder frame buffer platform 24, a climbing ladder 28, a tank top guardrail 29, a jack 43 and a traction rod 44; the horizontal support 53 is a frame support in the horizontal direction, the whole horizontal support 53 is rectangular, the length of the rectangle of the horizontal support 53 is 2-10 m, the width of the rectangle of the horizontal support is 1-5 m, the steel pipes used on four sides of the rectangle are the same, the thickness of the wall of each steel pipe is 5-10 mm, the cross section of the inner cavity of each steel pipe is rectangular, the length of the rectangle of the inner cavity of each steel pipe is 5-10 cm, the width of the rectangle of the inner cavity of each steel pipe is 4-6 cm, and the steel pipes on the four sides are connected into a whole at four corners of the rectangle through welding to form the horizontal support 53; the inclined strut steel frames 22 are supports for supporting and fixing the support cylinder frame 9, the number of the inclined strut steel frames is 4, the lower end of each inclined strut steel frame 22 is welded at one angle of the horizontal support 53, the upper end of each inclined strut steel frame is welded at the upper edge of the support cylinder frame 9, the cross section of each inclined strut steel frame 22 is an isosceles triangle, the bottom edge of the isosceles triangle is arranged at the inner side, the vertex angle of the isosceles triangle is arranged at the outer side, the waist of the isosceles triangle is arranged above the outer side edge of the steel pipe of the horizontal support 53, the length of the waist of the isosceles triangle is 5-20 cm, and the vertex angle of the isosceles triangle is welded above the angle of the horizontal support 53; the support frame 9 is an inverted frustum-shaped steel cylinder, the upper part of the inverted frustum-shaped lower half part of the reaction tank 4 is arranged in the support frame 9 and is fixed by the support frame 9, the diameter of the upper end circle of the support frame 9 is 1-5 m, the diameter of the lower end circle of the support frame 9 is 0.5-3 m, and the thickness of the wall of the support frame 9 is 0.5-1 cm; the support frame buffer 24 is a steel pipe support at the upper opening edge of the support frame 9, the support frame buffer 24 comprises two parts, namely a lookout buffer and a hoop buffer, the lookout buffer is a buffer extending out from the upper end of an inverted-frustum-shaped steel cylinder of the support frame 9, the lower parts of the two side walls of the lookout buffer are supported by steel plates welded on the outer surface of the support frame 9 through side walls, the two ends of the outer side wall of the lookout buffer are respectively welded with the upper end of the inclined strut steel frame 22, and a climbing ladder 28 penetrates through the center of the lookout buffer; the hoop buffering table is arranged on the periphery of the lower edge of the upper part of the reaction tank 4 and consists of steel pipes with the width of 10-20 cm and the upper and lower thickness of 5-10 cm, and the thickness of the steel pipe wall of the hoop buffering table is 0.5-1 cm; the supporting frame reinforcing rib 23 is a steel pipe welded on the outer surface of the supporting frame 9, is arranged in the vertical direction and plays a reinforcing role on the supporting frame 9, the upper end of the supporting frame reinforcing rib 23 is welded on the lower surface of a hoop buffering table of the supporting frame buffering table 24, the lower end of the supporting frame reinforcing rib 23 is welded on the steel pipe on the lower opening edge of the supporting frame 9, the cross section of the supporting frame reinforcing rib 23 is rectangular, the length of the rectangular supporting frame reinforcing rib 23 is 3-5 cm, the width of the rectangular supporting frame reinforcing rib is 2-3 cm, and the thickness of the steel pipe wall is 0.5-1 cm; the structure and the function of the support wheel 17 are the same as those of a commercially available rubber tire wheel, the upper end of the support wheel 17 is welded below one side wall of the horizontal support 53, the whole device can move under the dragging of a tractor and other traction equipment, the support wheel 17 comprises a support wheel support handle 18 and a support wheel body 19, the support wheel support handle 18 is a steel rod between the support wheel body 19 and the horizontal support 53, the length is 20-50 cm, the cross section of the support wheel support handle 18 is rectangular, and the rectangular length of the support wheel support handle 18 is 5-10 cm, and the width is 2-5 cm; the support wheel body 19 is a rotatable part of the support wheel 17, a rotating shaft is arranged in the center, a bearing is arranged outside the rotating shaft, a wheel hub is arranged outside the bearing, a tire is arranged outside the wheel hub, the tire is made of rubber and is divided into an inner tire and an outer tire, and air is filled into the inner tire. The H support 21 is a support which is H-shaped in the middle of the horizontal support 53 and can support the material crushing machine 1, the material receiving punching hopper 35 and the liquid guide groove 20, two ends of the left side arm and the right side arm of the H support 21 are welded on the front support and the rear support of the horizontal support 53, the left side arm and the right side arm are made of connecting steel pipes, the width of each connecting steel pipe is 10-20 cm, the upper surface of each connecting steel pipe is welded with the material crushing machine 1, the lower edge of the outer surface of the right side arm of the H support 21 is welded with the upper edges of the side walls of the material receiving punching hopper 35 and the liquid guide groove 20, and the material receiving punching hopper 35 and the liquid guide groove 20 are fixed together with the material receiving punching hopper support 15. The material receiving flushing hopper 35 is positioned below the right end of the material crushing machine 1, organic matter liquid and straw fragments coming out of the material crushing machine 1 can be received by the material receiving flushing hopper 35, and under the action of water flow sprayed into the material receiving flushing hopper 35 through the water spray pipe 14, the organic matter liquid and the straw fragments can be flushed into the saline-alkali wetland along with the liquid flow. One end of the receiving hopper 35 is plugged by a steel plate, one half of the other end is plugged by a steel plate, the other half is communicated with the liquid guide groove 20, and the end of the receiving hopper 35 with the plug is provided with an opening of the pipette 16 and an opening of the spray pipe 14; the liquid guide groove 20 is a groove with a U-shaped cross section, the bottom wall and the side wall are both made of steel plates, and the thicknesses of the steel plates used by the material receiving hopper 35 and the wall of the liquid guide groove 20 are both 2-5 mm. The material receiving punching bucket bracket 15 is a steel pipe for supporting the material receiving punching bucket 35, one end of the steel pipe is welded on the inner surface of the right side arm of the horizontal bracket 53, the other end of the steel pipe is welded on the right side wall of the material receiving punching bucket 35, the inner cavity of the cross section of the steel pipe is rectangular, the length of the rectangle is 3-5 cm, the width of the rectangle is 2-4 cm, and the thickness of the wall of the steel pipe is 0.5-1 cm. The draw bar 44 is a solid steel bar with one end welded at the center of the outer surface of the left arm of the horizontal bracket 53 and the other end free, the cross section of the draw bar 44 is rectangular, the length of the rectangle is 5-10 cm, the width is 4-6 cm, when the organic material processing equipment needs to move, the whole equipment is connected with the plug of the tractor and other traction equipment through the draw bar jack 43 by leaning against the draw bar 44 to draw together; the draw bar jack 43 is a cylindrical hole and is arranged at the free end of the draw bar 44, and the diameter of the round cross section of the draw bar jack 43 is 3-5 cm, and the height is 4-6 cm. The liquid adding pump 3 is a water pump which utilizes an electric water pump to pump water from the material receiving hopper 35 into the reaction tank 4 to provide water for decomposing straw, the structure and function of the liquid adding pump are the same as those of the electric water pump sold in the market, the electric power is supplied by a main power line 12, the liquid adding pump 3 is arranged on a horizontal bracket 53, and the liquid adding pump comprises a liquid adding pipe 8 and a liquid absorbing pipe 16. The liquid adding pipe 8 is a water pipe at the upper part of the liquid adding pump 3, one end of the liquid adding pipe is communicated with the pump body of the liquid adding pump 3, the other end of the liquid adding pipe is free, the opening is arranged at a tank top feed inlet 33 at the top of the reaction tank 4, the middle part of the liquid adding pipe is fixed on the outer surface of the upper part of the reaction tank 4 in the vertical direction through a fixing ring, the liquid adding pipe 8 is made of rubber, the wall thickness is 0.5-1 cm, a spiral steel wire is embedded in the wall, the cross section of the steel wire is circular, the diameter of the circle is 2-5 mm, and the pipe diameter of the inner cavity of the liquid adding pipe 8 is 5-10 cm; the pipette 16 is a pipeline for sucking water out of the receiving hopper 35 under the suction of the pump body of the liquid adding pump 3, the pipette 16 is made of rubber, the wall thickness is 0.5-1 cm, a spiral steel wire is embedded in the wall, the cross section of the steel wire is circular, the diameter of the circular steel wire is 2-5 mm, the diameter of an inner cavity of the pipette 16 is 5-10 cm, one end of the pipette 16 is communicated with the pump body of the liquid adding pump 3, the other end of the pipette 16 extends to the bottom of the receiving hopper 35, and the end, at the bottom of the receiving hopper 35, of the pipette 16 is provided with a faucet for ensuring that the liquid adding pump 3 can smoothly suck liquid from the bottom of the receiving hopper 35. The water pump 10 is a water pump which uses an electric water pump to pump water from a water source such as a ditch into the material receiving hopper 35 and wash organic matter liquid and straw crushing water which come out from the crusher 1 at the lower part of the reaction tank 4 for the reaction tank 4, the structure and the function of the water pump are the same as those of a commercially available electric water pump, the electric water pump is supplied with electric energy by a main power cord 12 and is arranged on a horizontal support 53, and the water pump 10 comprises a water suction pipe 11 and a water spray pipe 14. The spray pipe 14 is a water pipe at the upper part of the water pump 10, one end of the spray pipe is communicated with the pump body of the water pump 10, the other end of the spray pipe is free, the opening is arranged at the position of the blocking wall of the receiving hopper 35, the middle part of the spray pipe is transversely arranged between the horizontal bracket 53 and the receiving hopper 35, the spray pipe 14 is a steel pipe, the wall thickness is 0.5-1 cm, and the pipe diameter of an inner cavity is 5-10 cm; the water suction pipe 11 is a pipeline for sucking water from water sources such as ditches and the like into the material receiving hopper 35 under the suction of the pump body of the water suction pump 10, the water suction pipe 11 is made of rubber, the wall thickness is 0.5-1 cm, spiral steel wires are embedded in the wall of the water suction pipe 11, the cross section of each steel wire is circular, the diameter of each steel wire is 2-5 mm, the pipe diameter of an inner cavity of the water suction pipe 11 is 5-10 cm, one end of the water suction pipe 11 is communicated with the pump body of the liquid feeding pump 3, the other end of the water suction pipe extends into the water sources such as the ditches and the like, and a faucet is arranged at the end of the water suction pipe 11 in the water sources such as the ditches and the like and used for ensuring that the water suction pump 10 can smoothly suck water from the water sources such as the ditches and the like. The reaction tank 4 is a tank body which provides a suitable environment for straw crushing and bacterial liquid growth, the top of the reaction tank is provided with a tank top slow platform 5, a stirring motor 30, a baffle wall 31, a tank top feeding hole 33 and a tank top guardrail 29, the inside of the reaction tank is provided with a heating pipe 7 and a stirring rod 26, and the outer surface of the side wall of the reaction tank 4 at the central position of the extending part of the support rack slow platform 24 is provided with a climbing ladder 28; the tank top buffering platform 5 is a part between the tank top feeding hole 33 and the periphery of the top of the reaction tank 4 and is used for arranging a driving belt supporting rod 42, so that the liquid feeding pipe 8 and the driving belt discharging barrel 34 are better arranged and a moving space is provided for an operator; the climbing ladder 28 is a ladder for people to climb to the reaction tank 4, is made of steel, two side arms are made of round steel tubes, the thickness of the wall of each round steel tube is 2-5 mm, the diameter of the excircle of the cross section of each round steel tube is 3-5 cm, the upper ends of the two side arms are welded on the side edges of the top wall of the reaction tank 4, the middle of each side arm is welded in a lookout buffer of the support frame buffer 24, the lower end of each side arm is free, a cross rod in the middle of each two side arms is a flat steel tube, the horizontal direction of each flat steel tube is 5-10 cm, and the vertical direction of each flat steel tube is 1-2 cm; the baffle wall 31 is a raised steel plate at the inner side of the tank top feed port 33, the lower edge of the baffle wall is welded on the top wall of the reaction tank 4 at the edge of the tank top feed port 33, the upper edge is free, the highest position is 50-100 cm away from the upper surface of the top wall of the reaction tank 4, and the thickness of the steel plate of the baffle wall 31 is 0.5-1 cm; the hinge seal plate 6 is a steel plate which can be turned around a shaft in the tank top feed port 33 on the top wall of the reaction tank 4, two sides of the center of the hinge seal plate 6 are respectively provided with 1 rotating shaft under normal conditions, the rotating shafts can extend into bearings welded on two side walls of the tank top feed port 33 on the top wall of the reaction tank 4, so that the rotating shafts can rotate in the bearings, under normal conditions, the hinge seal plate 6 just blocks the tank top feed port 33 under no external pressure, but after a heavy object presses the upper surface of the hinge seal plate 6, the hinge seal plate 6 is turned, so that the tank top feed port 33 is exposed, and the heavy object automatically slides into the reaction tank 4; the opening of the tank top feeding hole 33 is sealed by a turnable hinge sealing plate 6, the hinge sealing plate 6 is turned under the water flow conveyed by a liquid feeding pipe 8 at the upper part of the liquid feeding pump 3 and the straw crushing pressure conveyed by a conveyor belt discharging barrel 34, the tank top feeding hole 33 is opened, water and straw fragments can enter the reaction tank 4, and bacteria liquid mate required by straw decomposition can be added to the liquid suction pipe 16 in the material receiving hopper 35 when the liquid feeding pump 3 works and are conveyed into the reaction tank 4 by the liquid feeding pump 3; the reaction tank 4 is divided into an upper part and a lower part, the upper part of the reaction tank 4 is cylindrical, the diameter of the cylinder is 1-5 meters, and the height of the cylinder is 2-5 meters; the lower part of the reaction tank 4 is in an inverted frustum shape, the diameter of the upper end circle of the inverted frustum shape of the reaction tank 4 is 1-5 m, the diameter of the lower end circle of the inverted frustum shape of the reaction tank 4 is 0.5-3 m, the lower end of the reaction tank 4 is communicated with the material crushing machine 1, the central cavity of the upper part and the lower part in the reaction tank 4 is a reaction tank cavity 25, the reaction tank cavity 25 is integrated, and no partition plate is arranged in the middle; the wall of the reaction tank 4 is made of steel, and the thickness is 0.5-2 cm; the heating pipe 7 is a part for heating materials in the whole reaction tank cavity 25, the temperature is controlled by the controller, the temperature range is the growth temperature range suitable for the high cellulose decomposition active bacteria, generally set to be 36.5-37.5 ℃, when the thermometer detects that the temperature of the reaction tank 4 is higher than the temperature range, the power supply can be automatically cut off, the heating is stopped, and when the thermometer detects that the temperature of the reaction tank 4 is lower than the temperature range, the heating pipe 7 can be automatically started to heat the reaction tank 4; the heating pipe 7 is in a U shape with an upward opening, two side arms are fixed on the opposite positions of the inner surface of the wall of the reaction tank 4, the bottom of the heating pipe is positioned in a reaction tank cavity 25 at the intersection of the upper part and the lower part of the reaction tank 4, the outer wall of the heating pipe 7 is a copper pipe, the thickness of the wall of the copper pipe is 0.5-1 mm, a heating resistance wire is arranged in the heating pipe, the power of the heating resistance wire is determined according to the size of the reaction tank 4, and the larger the reaction tank 4 is, the higher the power of the heating resistance wire is; the resistance wire is connected by ceramic cutting blocks, so that the resistance wire is not directly connected with the copper pipe wall, heat generated by the resistance wire can be released into the reaction tank cavity 25 through the copper pipe wall, and the resistance wire can be ensured not to be connected with electricity, and potential safety hazards to personnel contacting the tank body can be avoided. The stirring rod 26 is a component for stirring bacteria liquid required by water, straw fragments and straw decomposition and a fermentation body formed by the bacteria liquid companion so as to facilitate better and rapid growth of bacteria, the stirring rod 26 is made of steel and has a circular cross section, the diameter of the circular shape of the stirring rod 26 is 1-5 cm, the distance between two ends of the stirring rod 26 and the inner surface of the tank body of the reaction tank 4 is 10-20 cm, the stirring rod 26 is fixedly connected with a stirring motor rotating shaft 27 at the center and can horizontally rotate in the reaction tank cavity 25 under the drive of the stirring motor rotating shaft 27, and then liquid in the reaction tank cavity 25 is driven to be stirred. The stirring motor rotating shaft 27 is a steel shaft which can rotate under the drive of a stirring motor 30 rotor, the upper end of the stirring motor rotating shaft 27 extends to the center of a differential mechanism at the lower part of the stirring motor 30, the lower end of the stirring motor rotating shaft 27 is fixedly connected with the stirring rod 26, the stirring motor rotating shaft 27 is made of steel, the cross section of the stirring motor rotating shaft 27 is circular, and the diameter of the circle of the stirring motor rotating shaft 27 is 2-5 cm, and the length of the circle of the stirring motor rotating shaft 27 is 1-3 m; the stirring motor 30 is arranged in the center of the top of the reaction tank 4, the structure and the function of the stirring motor are the same as those of a commercially available motor, a differential mechanism is arranged at the bottom of the reaction tank, the speed of a rotor which rotates quickly by the stirring motor 30 can be reduced, the rotating speed of a rotating shaft 27 of the stirring motor can be adjusted as required, the stirring motor 30 is integrally cylindrical, and the diameter of the cylindrical cross section of the stirring motor 30 is 30-100 cm, and the height of the cylindrical cross section of the stirring motor 30 is 30-50 cm; the stirring motor 30 is powered by a stirring motor power line 32, the stirring motor power line 32 is a double-strand copper core power line, the cross section of the copper core is circular, the diameter of the copper core of the stirring motor power line 32 is 2-5 mm, one end of the stirring motor power line 32 is connected with the stirring motor 30, and the other end of the stirring motor power line 32 is connected with the main power line 12. The total power line 12 is a double-strand copper core power line, the cross section of the copper core is circular, and the diameter of the copper core of the total power line 12 is 3-8 mm. The main power line plug 13 is a three-phase plug, is arranged at the free end of the main power line 12, and can transmit the electric energy of an external power socket to organic material processing equipment used in the method for rapidly supplementing organic matters required in the saline-alkali wetland restoration process by using high cellulose decomposition active bacteria after being inserted into the external power socket. The structure and the function of the pulverizer 41 are the same as those of a commercially available straw pulverizer, various straws can be pulverized into straw pieces, a mincing roller is arranged in the pulverizer 41, the base part of the pulverizer 41 is cuboid, the cuboid at the base part of the pulverizer 41 is 2-4 meters long, 1-1.5 meters wide and 0.5-1 meter high, 4 rollers are arranged at the lower part of the cuboid at the base part of the pulverizer 41 so as to move the whole pulverizer 41, the mincing roller can pulverize the straws coming from the feeding port 38 of the pulverizer under the driving of a motor of the pulverizer 41, an air blowing structure is arranged in the pulverizer 41, and the air blowing structure can blow out the pulverized straw pieces to blow the straw pieces onto the conveyor belt 40 of the conveyor belt receiving platform 39 from the discharging nozzle 37 of the pulverizer; the crusher feed port 38 is a square opening where various straw can be stuffed into the crusher 41; the crusher discharging nozzle 37 is a flat tube structure on the upper part of the crusher 41 opposite to the crusher feeding port 38, the crusher discharging nozzle 37 has a large and rectangular base opening, the rectangular length is 1-1.5 m, the width is 10-30 cm, the crusher discharging nozzle 37 has a small and oval free end opening, the oval long diameter is 10-30 cm, the short diameter is 10-15 cm, and the crusher discharging nozzle 37 has an opening positioned on the conveyor belt 40. The conveying belt 40 is a structure for conveying the straw pieces processed by the pulverizer 41 into the reaction tank 4, the structure and the function of the conveying belt are the same as those of a known conveying belt, and the conveying belt comprises a conveying belt discharging cylinder 34, a conveying belt surrounding cylinder 36, a conveying belt receiving platform 39 and a conveying belt supporting rod 42, wherein the conveying belt discharging cylinder 34 is a bent cylinder at the top of the conveying belt 40, the wall of the conveying belt discharging cylinder 34 is made of steel, and the thickness of the conveying belt discharging cylinder is 1-5 mm; the base part of the conveyor belt discharging cylinder 34 is communicated with the conveyor belt surrounding cylinder 36, the end part is free, the opening is arranged above the tank top feeding hole 33, under the action of gravity, straw pieces conveyed by the conveyor belt 40 fall onto the turnable hinge sealing plate 6 from the free end opening of the conveyor belt discharging cylinder 34, the hinge sealing plate 6 is pressed to turn over, and then the straw pieces fall into the reaction tank 4; the conveying belt surrounding cylinder 36 is positioned between the conveying belt discharging cylinder 34 and the conveying belt receiving platform 39 and is cylindrical, the diameter of the cylinder is 30-50 cm, the wall of the conveying belt surrounding cylinder 36 is made of steel, the thickness of the cylinder is 1-5 mm, a belt capable of rotating back and forth is arranged inside the conveying belt surrounding cylinder 36, and the rotation of the belt can convey the straw fragments from the conveying belt receiving platform 39 to the conveying belt discharging cylinder 34; the driving belt supporting rod 42 is made of steel and has a circular cross section, the center of the lower surface of the upper end of the driving belt surrounding barrel 36 is the supporting rod, and the diameter of the driving belt supporting rod 42 is 3-10 cm, and the height of the driving belt supporting rod is 0.3-0.5 m; the conveyor belt receiving platform 39 is horizontally arranged, 4 rollers are arranged at the lower part of the conveyor belt receiving platform, so that the whole conveyor belt 40 can move under the action of dragging force, and a horizontal belt is arranged at the upper part of the conveyor belt receiving platform 39 and can smoothly receive straw scraps falling from the opening of the discharge nozzle 37 of the pulverizer.
The foregoing shows and describes the general principles and broad features of the present invention and advantages thereof. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are merely illustrative of the principles of the invention, but that various changes and modifications may be made without departing from the spirit and scope of the invention, which is defined by the appended claims and their equivalents.

Claims (7)

1.利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，是在盐碱湿地有水处，设置多个可移动的有机质料加工设备，在有机质料加工设备中先将秸秆粉碎，然后将粉碎料输送到反应罐中，在反应罐内同时加入反应液，所述的反应液为水、高纤维素分解活性菌、能够促进高纤维素分解活性菌发挥活性的菌液伴侣三种成份所组成，三种成份的比例为95：1：4，其中，高纤维素分解活性菌是所有对纤维素具有分解活性的细菌、放线菌或真菌，不论哪类菌，所用菌为单一菌种或者多种菌的混合液；能够促进高纤维素分解活性菌发挥活性的菌液伴侣则是尿素、氨水或碳酸氢铵，实验证明这些氮肥能够显著促进高纤维素分解活性菌活性的发挥；粉碎秸秆在反应罐内反应时，要加热和搅拌，以促进秸秆的分解速度；秸秆分解后形成的有机质则在抽水泵喷水管喷出水的冲刷下，从与接料冲斗后端相连的导液槽流出到盐碱湿地中，顺着盐碱湿地的水渠漫灌到盐碱湿地的每一个角落，由于秸秆块在反应罐中腐熟分解较彻底，10天即可分解80％以上，几乎都变成了有机质，因此当腐熟分解后的有机质从导液槽释放出来后，沿着盐碱湿地内的沟渠被浇灌到盐碱湿地后，从而达到为待修复盐碱湿地快速为盐碱湿地补充盐碱湿地修复过程中所需有机质的目的；所用的有机质料加工设备由碎料机(1)、支撑钢架(2)、加液泵(3)、反应罐(4)、罐顶缓台(5)、合页封板(6)、加热管(7)、抽水泵(10)、总电源线(12)、总电源线插头(13)、导液槽(20)、搅拌棒(26)、搅拌电机转轴(27)、罐顶护栏(29)、搅拌电机(30)、遮挡墙(31)、接料冲斗(35)、传送带(40)、粉碎机(41)组成，其特征在于：所述的反应罐(4)是为秸秆碎和菌液生长提供适宜环境的罐体，顶部设置有罐顶缓台(5)、搅拌电机(30)、遮挡墙(31)、罐顶进料口(33)和罐顶护栏(29)，内部设置有加热管(7)和搅拌棒(26)，在支筒架缓台(24)伸出部分中央位置的反应罐(4)侧壁外表面设置攀登梯(28)；罐顶缓台(5)是罐顶进料口(33)与反应罐(4)顶部周缘之间的部分；攀登梯(28)是供人攀爬到反应罐(4)的梯子，为钢质，两侧臂为圆钢管制成，圆钢管壁的厚度为2-5毫米，圆钢管横截面外圆的直径为3-5厘米，两侧臂上端焊接在反应罐(4)顶壁侧缘，中间焊接在支筒架缓台(24)的瞭望缓台内，下端游离，两侧臂中间的横杆为扁钢管，扁钢管水平方向的宽度为5-10厘米，上下方向的厚度为1-2厘米；遮挡墙(31)是罐顶进料口(33)内侧的凸起钢板，下缘焊接在罐顶进料口(33)边缘的反应罐(4)顶壁上，上缘游离，最高处距离反应罐(4)顶壁上表面50-100厘米，遮挡墙(31)钢板的厚度为0.5-1厘米；合页封板(6)中央两侧各有1个转轴，转轴可伸入焊接在反应罐(4)顶壁罐顶进料口(33)两侧壁上的轴承内，使得转轴能够在轴承内转动；罐顶进料口(33)由可翻动的合页封板(6)封住开口；反应罐(4)分为上下两部分，反应罐(4)上部呈圆筒形，圆筒的直径为1-5米、高度为2-5米；反应罐(4)下部呈倒圆台形，反应罐(4)倒圆台形上端圆直径为1-5米、下端圆直径为0.5-3米，反应罐(4)下端与碎料机(1)相连通，反应罐(4)内部上下两部分中央的空腔为反应罐腔(25)，反应罐腔(25)一个整体，中间没有任何隔板；反应罐(4)的壁为钢质，厚度为0.5-2厘米；加热管(7)是为整个反应罐腔(25)内的材料加热的部件，由控制器控制温度的大小，温度范围是高纤维素分解活性菌适宜的生长温度范围，温度范围为36.5-37.5℃；加热管(7)呈开口朝上的U字形，两侧臂固定在反应罐(4)壁内表面相对的位置上，底部处于反应罐(4)上下部分交汇处的反应罐腔(25)里，加热管(7)外壁为铜管，铜管壁的厚度为0.5-1毫米，管内为加热电阻丝，反应罐(4)越大，加热电阻丝的功率也就越大；电阻丝被陶瓷质的分割块相连；搅拌棒(26)为钢质，横截面呈圆形，搅拌棒(26)圆形的直径为1-5厘米，搅拌棒(26)两端距离反应罐(4)罐体内表面10-20厘米，搅拌棒(26)在中央处与搅拌电机转轴(27)固定连接在一起；搅拌电机转轴(27)是搅拌电机(30)转子带动下能够转动的钢轴，上端伸到搅拌电机(30)下部的差速器中央，下端与搅拌棒(26)固定连接在一起，搅拌电机转轴(27)为钢质，横截面呈圆形，搅拌电机转轴(27)圆形的直径为2-5厘米、长度为1-3米；搅拌电机(30)设置在反应罐(4)顶部中央，在底部设置一个差速器，搅拌电机(30)整体呈圆柱形，搅拌电机(30)圆柱形横截面圆形的直径为30-100厘米、高度为30-50厘米；搅拌电机电源线(32)为双股铜芯电源线，铜芯横截面为圆形，搅拌电机电源线(32)铜芯的直径为2-5毫米，搅拌电机电源线(32)一端连接搅拌电机(30)、另一端连接总电源线(12)。1. The method of using high cellulolytic active bacteria to quickly replenish the organic matter required in the process of saline-alkali wetland restoration is to set up multiple movable organic material processing equipment where there is water in the saline-alkali wetland. The straw is pulverized, then the pulverized material is transported to the reaction tank, and a reaction solution is added to the reaction tank at the same time, and the reaction solution is water, high cellulolytic activity bacteria, and bacteria that can promote the activity of high cellulolytic active bacteria The liquid partner is composed of three components, and the ratio of the three components is 95:1:4. Among them, the high cellulolytic activity bacteria are all bacteria, actinomycetes or fungi that have decomposition activity on cellulose, no matter what kind of bacteria, The bacteria used are a single strain or a mixture of multiple bacteria; the bacterial partners that can promote the activity of high cellulolytic bacteria are urea, ammonia or ammonium bicarbonate. Experiments have shown that these nitrogen fertilizers can significantly promote high cellulolytic activity. When the pulverized straw is reacted in the reaction tank, it should be heated and stirred to promote the decomposition rate of the straw; the organic matter formed after the decomposition of the straw will be washed by the water sprayed from the water pump spray pipe, and the material will be mixed with the material. The diversion tank connected to the back end of the bucket flows out into the saline-alkali wetland, and floods every corner of the saline-alkali wetland along the water channel of the saline-alkali wetland. Since the straw blocks are decomposed thoroughly in the reaction tank, they can be decomposed in 10 days. More than 80% of the organic matter has become organic matter. Therefore, when the decomposed organic matter is released from the diversion tank, it is irrigated into the saline-alkali wetland along the ditches in the saline-alkali wetland, so as to achieve the goal of restoring the saline-alkali wetland. The purpose of quickly supplementing the saline-alkali wetland with the organic matter required in the restoration process of the saline-alkali wetland; the organic material processing equipment used consists of a crusher (1), a supporting steel frame (2), a liquid addition pump (3), and a reaction tank (4). ), tank top stage (5), hinge sealing plate (6), heating pipe (7), water pump (10), mains power cord (12), mains power cord plug (13), liquid conduit (20) ), stirring rod (26), stirring motor shaft (27), tank top guardrail (29), stirring motor (30), blocking wall (31), receiving bucket (35), conveyor belt (40), pulverizer ( 41) composition, it is characterized in that: the reaction tank (4) is a tank body that provides suitable environment for the growth of straw fragments and bacterial liquid, and the top is provided with a tank top retarder (5), a stirring motor (30), a shielding wall (31), the tank top feeding port (33) and the tank top guardrail (29), a heating pipe (7) and a stirring rod (26) are arranged inside, and the center position of the extended part of the support cylinder rack (24) A climbing ladder (28) is arranged on the outer surface of the side wall of the reaction tank (4); the tank top stage (5) is the part between the tank top feeding port (33) and the top periphery of the reaction tank (4); the climbing ladder (28) It is a ladder for people to climb to the reaction tank (4). It is made of steel. The arms on both sides are made of round steel pipes. cm, the upper ends of the arms on both sides are welded to the side edges of the top wall of the reaction tank (4), the middle is welded in the observation platform of the support cylinder support platform (24), the lower ends are free, and the horizontal bars in the middle of the arms are flat steel pipes. Steel Pipe The width in the horizontal direction is 5-10 cm, and the thickness in the vertical direction is 1-2 cm; the shielding wall (31) is a raised steel plate on the inner side of the tank top feeding port (33), and the lower edge is welded to the tank top feeding port ( 33) On the top wall of the reaction tank (4) on the edge, the upper edge is free, the highest point is 50-100 cm from the upper surface of the top wall of the reaction tank (4), and the thickness of the steel plate of the shielding wall (31) is 0.5-1 cm; The sealing plate (6) has a rotating shaft on both sides of the center, and the rotating shaft can extend into the bearings welded on the two side walls of the inlet (33) of the top wall of the reaction tank (4), so that the rotating shaft can rotate in the bearing. ; The feeding port (33) on the top of the tank is sealed by a hinged sealing plate (6) that can be turned over; the reaction tank (4) is divided into upper and lower parts, the upper part of the reaction tank (4) is cylindrical, and the diameter 1-5 meters, height 2-5 meters; the lower part of the reaction tank (4) is in the shape of an inverted truncated cone, the diameter of the upper circle of the inverted truncated cone of the reaction tank (4) is 1-5 meters, and the diameter of the lower circle is 0.5-3 meters, The lower end of the reaction tank (4) is communicated with the crusher (1). The cavity in the center of the upper and lower parts of the reaction tank (4) is the reaction tank cavity (25). The reaction tank cavity (25) is a whole without any partition in the middle. plate; the wall of the reaction tank (4) is made of steel, with a thickness of 0.5-2 cm; the heating pipe (7) is a component for heating the material in the entire reaction tank cavity (25), and the temperature is controlled by the controller. The range is the suitable growth temperature range of high cellulolytic activity bacteria, and the temperature range is 36.5-37.5 ° C; In terms of position, the bottom is in the reaction tank cavity (25) where the upper and lower parts of the reaction tank (4) meet, the outer wall of the heating pipe (7) is a copper pipe, the thickness of the copper pipe wall is 0.5-1 mm, and the inside of the pipe is a heating resistance wire, The larger the reaction tank (4) is, the greater the power of the heating resistance wire; the resistance wire is connected by the ceramic dividing blocks; the stirring rod (26) is made of steel, the cross section is circular, and the stirring rod (26) is circular The diameter of the stirring rod (26) is 10-20 cm from the inner surface of the reaction tank (4), and the stirring rod (26) is fixedly connected with the stirring motor shaft (27) at the center; stirring The motor shaft (27) is a steel shaft that can be rotated by the rotor of the stirring motor (30), the upper end extends to the center of the differential at the lower part of the stirring motor (30), and the lower end is fixedly connected with the stirring rod (26). (27) is made of steel, the cross section is circular, and the circular diameter of the stirring motor shaft (27) is 2-5 cm and the length is 1-3 meters; the stirring motor (30) is arranged in the center of the top of the reaction tank (4) , a differential is arranged at the bottom, the stirring motor (30) is cylindrical as a whole, and the circular diameter of the cylindrical cross-section of the stirring motor (30) is 30-100 cm and the height is 30-50 cm; the stirring motor power cord ( 32) is a double-stranded copper core power cord, the cross section of the copper core is circular, the diameter of the copper core of the stirring motor power cord (32) is 2-5 mm, and one end of the stirring motor power cord (32) is Connect the stirring motor (30) and the other end to the mains power line (12). 2.根据权利要求1所述的利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，其特征在于：所述的碎料机(1)一端设置一个电动机、中间为螺旋搅动推进舱、另一端为剪切板、剪切板外面为清理刀(52)；碎料机(1)的电动机整体呈圆柱形，碎料机(1)的电动机圆柱的横截面圆形的直径为10-50厘米、高度为10-30厘米，电动机的转子与螺旋搅动推进舱内的螺旋轴相连在一起，成为一个整体，电动机的转子的转动能够轻松带动螺旋轴随之转动，电动机固定在H支架(21)中央上表面的一侧，由与之连接的总电源线(12)分支电源线供应电能，螺旋搅动推进舱固定在H支架(21)中央的上表面，螺旋搅动推进舱一端与电动机焊接在一起，另一端则固定在H支架(21)中央上表面的另一侧；碎料机(1)的剪切板是双层圆板，为锰钢质，双层圆板分别为砧板(45)和动板(49)，砧板(45)和动板(49)的厚度均为0.5-1厘米，砧板(45)在外、动板(49)在内，砧板(45)的直径等于螺旋搅动推进舱的内径，动板(49)的直径小于螺旋搅动推进舱的内径1-2毫米，砧板(45)周缘固定在螺旋搅动推进舱相对电动机另一端，砧板(45)的外表面与螺旋搅动推进舱该端外表面处于同一个平面内，砧板(45)中央设置一个砧板轴承(48)，砧板轴承(48)中央的空腔为砧板轴承腔(47)，砧板轴承腔(47)供转轴(51)穿过，使得砧板轴承(48)内环与转轴(51)固定在一起；转轴(51)内端与螺旋搅动推进舱内的螺旋轴相连在一起，并成为一个整体，转轴(51)为锰钢质，呈圆柱形，圆柱的横截面圆形的直径为2-10厘米，转轴(51)外端游离，并在外端表面对称连接有一对清理刀(52)；清理刀(52)为四棱柱状，四棱柱的横截面为正方形，正方形的边长为1-2厘米，清理刀(52)的长度为4-20厘米，一侧面与砧板(45)的外表面之间相距0.5-1毫米；在砧板轴承(48)外缘与砧板周缘所在板面的中央圆上，等间距设置多个圆形砧板释放孔(46)，砧板释放孔(46)的直径为0.5-1厘米，砧板释放孔(46)为直圆孔，呈圆柱形，砧板释放孔(46)内外两端周缘具有明显锐边，组成双层圆板能够剪切的不动边；动板(49)位于砧板(45)的内侧，固定在转轴(51)上，能够随转轴(51)的转动而转动，在转轴(51)表面与动板(49)周缘之间所在板面的中央圆上，等间距设置多个动板释放孔(50)；动板释放孔(50)和砧板释放孔(46)相对时，动板释放孔(50)的中央轴与砧板释放孔(46)的中央轴处于同一条直线上；动板释放孔(50)呈圆台形，圆台的上底朝外，与砧板释放孔(46)大小相同，圆台的下底朝内，所在圆直径为0.7-1.4厘米；螺旋搅动推进舱中央为螺旋轴，外部为圆筒形的舱壁，舱壁一端焊接在电动机的侧壁上，另一端游离，在游离端的开口处设置砧板(45)后被砧板(45)封堵，在舱壁顶部中央有一个圆形的开口，开口周缘与反应罐(4)下口周缘焊接在一起，反应罐(4)中的秸秆碎及有机质液体即可从该开口进入螺旋搅动推进舱中；螺旋搅动推进舱的螺旋轴的一端与碎料机(1)的电动机的转子连接在一起，螺旋轴的另一端与转轴(51)连接在一起，螺旋轴的外表面具有螺旋形的棱脊凸起；螺旋搅动推进舱外部为圆筒形的舱壁，舱壁为不锈钢质或铝合金质，厚度为1-5厘米，圆筒形的舱壁内腔横截面圆形的直径为8-40厘米、高度为20-100厘米。2. the method for utilizing high cellulolytic active bacteria to quickly replenish the required organic matter in the saline-alkali wetland repair process according to claim 1, is characterized in that: one end of described crusher (1) is provided with a motor, and the middle is The screw stirring propelling cabin, the other end is a shearing plate, and the outside of the shearing plate is a cleaning knife (52); the electric motor of the crusher (1) is cylindrical as a whole, and the cross-section of the motor cylinder of the crusher (1) is circular The diameter of the motor is 10-50 cm and the height is 10-30 cm. The rotor of the motor is connected with the screw shaft in the screw stirring propulsion cabin to form a whole. The rotation of the rotor of the motor can easily drive the screw shaft to rotate. It is fixed on one side of the central upper surface of the H bracket (21), and the branch power lines of the main power line (12) connected to it are supplied with electric power. One end of the cabin is welded with the motor, and the other end is fixed on the other side of the central upper surface of the H bracket (21). The boards are a chopping board (45) and a moving board (49), the thicknesses of the chopping board (45) and the moving board (49) are both 0.5-1 cm, the cutting board (45) is outside, the moving board (49) is inside, and the cutting board (45) ) is equal to the inner diameter of the screw agitation propelling cabin, the diameter of the moving plate (49) is 1-2 mm smaller than the inner diameter of the screw agitation propelling cabin, the periphery of the cutting board (45) is fixed on the other end of the screw stirring propelling cabin relative to the motor, and the cutting board (45) The outer surface of the helical stirring chamber is in the same plane as the outer surface of the end of the screw agitation propelling chamber. An anvil bearing (48) is arranged in the center of the anvil (45), and the cavity in the center of the anvil bearing (48) is an anvil bearing cavity (47). The cavity (47) is passed through by the rotating shaft (51), so that the inner ring of the anvil bearing (48) is fixed with the rotating shaft (51); the inner end of the rotating shaft (51) is connected with the screw shaft in the screw agitation propulsion cabin, and becomes As a whole, the rotating shaft (51) is made of manganese steel and has a cylindrical shape, the diameter of the circular cross section of the cylinder is 2-10 cm, the outer end of the rotating shaft (51) is free, and a pair of cleaning knives (52) are symmetrically connected on the outer end surface. ); the cleaning knife (52) is in the shape of a quadrangular prism, the cross section of the quadrangular prism is square, the side length of the square is 1-2 cm, the length of the cleaning knife (52) is 4-20 cm, and one side is connected to the cutting board (45) A distance of 0.5-1 mm is provided between the outer surfaces of the cutting board bearings (48) and the central circle of the board surface where the outer edge of the cutting board bearing (48) and the peripheral edge of the cutting board are located. The diameter of the cutting board is 0.5-1 cm, the cutting board release hole (46) is a straight circular hole and is cylindrical, and the inner and outer edges of the cutting board release hole (46) have obvious sharp edges, forming a fixed edge that can be cut by the double-layer circular board. The moving plate (49) is located on the inner side of the cutting board (45), is fixed on the rotating shaft (51), can rotate with the rotation of the rotating shaft (51), and is located between the surface of the rotating shaft (51) and the periphery of the moving plate (49) On the central circle of the face, set up multiple The moving plate releasing hole (50); when the moving plate releasing hole (50) and the cutting plate releasing hole (46) are opposite to each other, the central axis of the moving plate releasing hole (50) and the central axis of the anvil releasing hole (46) are on the same straight line ; The moving plate release hole (50) is in the shape of a circular truncated table, the upper bottom of the circular table faces outward, and is the same size as the cutting board release hole (46), and the lower bottom of the circular table faces inward, and the diameter of the circle is 0.7-1.4 cm; the center of the spiral stirring propelling cabin It is a screw shaft, and the exterior is a cylindrical bulkhead. One end of the bulkhead is welded to the side wall of the motor, and the other end is free. A chopping board (45) is set at the opening of the free end and then blocked by the chopping board (45). There is a circular opening in the center of the top, the periphery of the opening and the periphery of the lower mouth of the reaction tank (4) are welded together, and the broken straw and the organic matter liquid in the reaction tank (4) can enter the screw stirring propelling cabin through the opening; the screw stirring One end of the screw shaft of the propelling cabin is connected with the rotor of the electric motor of the crusher (1), the other end of the screw shaft is connected with the rotating shaft (51), and the outer surface of the screw shaft has a helical ridge protrusion; The exterior of the screw stirring propellant cabin is a cylindrical bulkhead, the bulkhead is made of stainless steel or aluminum alloy, the thickness is 1-5 cm, and the diameter of the circular cross-section of the cylindrical bulkhead cavity is 8-40 cm, Height is 20-100 cm. 3.根据权利要求1所述的利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，其特征在于：所述的支撑钢架(2)为钢质，能在拖拉机等牵引设备的拖拽下移动，用于支撑碎料机(1)、加液泵(3)、反应罐(4)和抽水泵(10)，顶部一通过传动带支杆(42)与传送带(40)连接在一起，支撑钢架(2)由水平支架(53)、斜撑钢架(22)、支筒架(9)、接料冲斗支架(15)、支架轮(17)、支架轮支柄(18)、支架轮体(19)、H支架(21)、支筒架加固棱(23)、支筒架缓台(24)、攀登梯(28)、罐顶护栏(29)、牵引杆插孔(43)、牵引杆(44)组成；水平支架(53)是水平方向的边框支架，整体呈长方形，水平支架(53)长方形的长度为2-10米、宽度为1-5米，长方形的四个边所用钢管均相同，钢管壁的厚度为5-10毫米，钢管内腔横截面呈长方形，钢管内腔长方形的长度为5-10厘米、宽度为4-6厘米，四个边的钢管在长方形四个角处通过焊接连接呈一个整体，共同构成水平支架(53)；斜撑钢架(22)是支撑固定支筒架(9)的支架，共4根，每根斜撑钢架(22)的下端焊接在水平支架(53)一个角处，上端焊接在支筒架(9)上缘，斜撑钢架(22)的横截面为等腰三角形，等腰三角形的底边在内侧、顶角在外侧，等腰三角形的腰位于水平支架(53)钢管外侧缘上方，等腰三角形腰的长度为5-20厘米，等腰三角形的顶角焊接在水平支架(53)的角上方；支筒架(9)是倒圆台形钢筒，反应罐(4)倒圆台形的下半部的上部即设置在支筒架(9)中，被支筒架(9)所固定，支筒架(9)上端圆直径为1-5米、下端圆直径为0.5-3米，支筒架(9)壁的厚度为0.5-1厘米；支筒架缓台(24)是支筒架(9)上口缘的钢管支架，支筒架缓台(24)包括两部分，一是瞭望缓台，二是环箍缓台，瞭望缓台是从支筒架(9)倒圆台形钢筒上端伸出的一个缓台，瞭望缓台两侧壁下方靠侧壁焊接在支筒架(9)外表面的钢板支撑，瞭望缓台外侧壁两端分别与斜撑钢架(22)的上端焊接在一起，瞭望缓台中央有攀登梯(28)从中穿过；环箍缓台则是设置在反应罐(4)上部下底缘周边，有宽度为10-20厘米、上下厚度为5-10厘米的钢管组成，环箍缓台钢管壁的厚度为0.5-1厘米；支筒架加固棱(23)是焊接在支筒架(9)外表面的钢管，上下方向设置，支筒架加固棱(23)上端焊接在支筒架缓台(24)的环箍缓台下表面，下端焊接在支筒架(9)下口缘的钢管上，支筒架加固棱(23)横截面呈长方形，支筒架加固棱(23)长方形的长度为3-5厘米、宽度为2-3厘米、钢管壁的厚度为0.5-1厘米；支架轮(17)包括支架轮支柄(18)和支架轮体(19)，支架轮支柄(18)是支架轮体(19)与水平支架(53)之间的钢杆，长度为20-50厘米，支架轮支柄(18)的横截面呈长方形，支架轮支柄(18)长方形的长度为5-10厘米、宽度为2-5厘米；支架轮体(19)是支架轮(17)能转动的部分，中央为转轴、转轴外是轴承、轴承外为轮毂、轮毂外为轮胎，轮胎橡胶质，又分内胎和外胎，空气即充进内胎里面；H支架(21)是水平支架(53)中间呈H形的支架，用于支撑碎料机(1)、接料冲斗(35)和导液槽(20)，H支架(21)左右两侧臂两端均焊接在水平支架(53)的前后支架上，左右两侧臂之间由连接钢管制成，连接钢管的宽度为10-20厘米，连接钢管上表面与碎料机(1)焊接在一起，H支架(21)右侧臂外表面下缘与接料冲斗(35)和导液槽(20)一侧壁的上缘焊接在一起；接料冲斗(35)一端由钢板封堵，另一端的一半由钢板封堵，剩下的另一半则与导液槽(20)相连通，接料冲斗(35)有封堵的这端设置有吸液管(16)的开口和喷水管(14)的开口；导液槽(20)为横截面呈U形的凹槽，底壁和侧壁均由钢板制成，接料冲斗(35)和导液槽(20)的壁所用钢板的厚度均为2-5毫米；接料冲斗支架(15)是支撑接料冲斗(35)的钢管，一端焊接在水平支架(53)右侧臂内表面，另一端焊接在接料冲斗(35)右侧壁上，钢管的横截面内腔呈长方形，长方形的长度为3-5厘米、宽度为2-4厘米，钢管壁的厚度为0.5-1厘米；牵引杆(44)是一端焊接在水平支架(53)左侧臂外表面中央、另一端游离的实心钢杆，牵引杆(44)的横截面呈长方形，长方形的长度为5-10厘米、宽度为4-6厘米；牵引杆插孔(43)为圆柱状孔，设置在牵引杆(44)的游离端，牵引杆插孔(43)圆柱横截面圆形的直径为3-5厘米、高度为4-6厘米；总电源线(12)为双股铜芯电源线，铜芯横截面为圆形，总电源线(12)铜芯的直径为3-8毫米；总电源线插头(13)是三相插头，设置在总电源线(12)的游离端。3. the method for utilizing high cellulolytic active bacteria to quickly replenish the required organic matter in the repairing process of saline-alkali wetlands according to claim 1, is characterized in that: described supporting steel frame (2) is steel, can be used in the tractor It is used to support the crusher (1), the liquid addition pump (3), the reaction tank (4) and the suction pump (10), and the top one passes through the transmission belt support rod (42) and the conveyor belt ( 40) Connected together, the support steel frame (2) consists of a horizontal support (53), a diagonal support steel frame (22), a support cylinder frame (9), a material receiving punch support (15), a support wheel (17), a support Wheel support handle (18), bracket wheel body (19), H bracket (21), support cylinder frame reinforcement edge (23), support cylinder frame buffer (24), climbing ladder (28), tank top guardrail (29) , the drawbar socket (43), and the drawbar (44); the horizontal bracket (53) is a horizontal frame bracket, and the overall shape is rectangular. 5 meters, the four sides of the rectangle use the same steel pipe, the thickness of the steel pipe wall is 5-10 mm, the cross section of the steel pipe cavity is rectangular, the length of the steel pipe cavity rectangle is 5-10 cm, and the width is 4-6 cm. The steel pipes on the four sides are connected by welding at the four corners of the rectangle to form a whole, and together form a horizontal support (53); the diagonal bracing steel frame (22) is a support for supporting the fixed support cylinder frame (9), a total of four, each The lower end of the diagonal bracing steel frame (22) is welded at a corner of the horizontal support (53), and the upper end is welded on the upper edge of the supporting cylinder frame (9). The base of the triangle is on the inside, the top corner is on the outside, the waist of the isosceles triangle is located above the outer edge of the horizontal support (53) steel pipe, the length of the isosceles triangle waist is 5-20 cm, and the top corner of the isosceles triangle is welded to the horizontal support Above the corner of (53); the support cylinder frame (9) is an inverted truncated truncated steel cylinder, and the upper part of the lower half of the inverted truncated truncated cone of the reaction tank (4) is set in the support cylinder frame (9), and is supported by the cylinder support (9). 9) to be fixed, the diameter of the upper end circle of the support cylinder frame (9) is 1-5 meters, the diameter of the lower end circle is 0.5-3 meters, and the thickness of the wall of the support cylinder frame (9) is 0.5-1 cm; 24) is the steel pipe bracket on the upper edge of the support cylinder frame (9). The support cylinder frame buffer platform (24) includes two parts, one is the observation buffer platform, and the second is the hoop buffer platform. The observation buffer platform is from the support cylinder frame (24). 9) A buffer platform protruding from the upper end of the rounded table-shaped steel cylinder, the bottom of the two side walls of the observation platform is supported by the steel plates welded on the outer surface of the support cylinder frame (9) by the side walls, and the two ends of the outer side wall of the observation platform are respectively connected with the diagonal braces. The upper ends of the steel frame (22) are welded together, and a climbing ladder (28) passes through the center of the observation buffer; the hoop buffer is arranged around the lower bottom edge of the upper part of the reaction tank (4), with a width of 10-20 cm, the upper and lower thickness of the steel pipe is 5-10 cm, the thickness of the hoop buffer steel pipe wall is 0.5-1 cm; the support cylinder frame reinforcement edge (23) is a steel pipe welded on the outer surface of the support cylinder frame (9). The direction is set, and the upper end of the reinforcing edge (23) of the support cylinder frame is welded to the support cylinder The lower surface of the hoop buffer of the frame buffer table (24), the lower end is welded on the steel pipe on the lower edge of the support cylinder frame (9), the cross section of the support cylinder frame reinforcement edge (23) is rectangular, and the support cylinder frame reinforcement edge (23) ) The length of the rectangle is 3-5 cm, the width is 2-3 cm, and the thickness of the steel pipe wall is 0.5-1 cm; the bracket wheel (17) includes the bracket wheel support handle (18) and the bracket wheel body (19), the bracket wheel The support handle (18) is a steel rod between the support wheel body (19) and the horizontal support (53), the length is 20-50 cm, the cross section of the support wheel support handle (18) is rectangular, and the support wheel support handle (18) ) The length of the rectangle is 5-10 cm and the width is 2-5 cm; the bracket wheel body (19) is the part that the bracket wheel (17) can rotate, the center is the rotating shaft, the outside of the rotating shaft is the bearing, the outside of the bearing is the hub, the outside of the hub is It is a tire, the tire is rubber, and it is divided into an inner tube and an outer tire, and the air is filled into the inner tube; the H bracket (21) is an H-shaped bracket in the middle of the horizontal bracket (53), which is used to support the crusher (1), the material receiving The punching bucket (35) and the liquid guiding groove (20), the left and right arms of the H bracket (21) are welded on the front and rear brackets of the horizontal bracket (53), and the left and right arms are made of connecting steel pipes, which are connected to each other. The width of the steel pipe is 10-20 cm, and the upper surface of the connecting steel pipe is welded with the crusher (1). ) The upper edges of one side wall are welded together; one end of the receiving punch (35) is sealed by steel plates, half of the other end is sealed by steel plates, and the other half is connected with the liquid guide groove (20), and the The end of the hopper (35) that is blocked is provided with the opening of the suction pipe (16) and the opening of the water spray pipe (14); the liquid guide groove (20) is a U-shaped groove in cross section, and the bottom wall is and the side walls are all made of steel plates, the thickness of the steel plates used for the walls of the receiving punch (35) and the liquid guide groove (20) are both 2-5 mm; the receiving punch bracket (15) is used to support the receiving punch The steel pipe of (35), one end is welded on the inner surface of the right arm of the horizontal support (53), and the other end is welded on the right side wall of the receiving punch (35). -5 cm, width 2-4 cm, thickness of steel pipe wall is 0.5-1 cm; drawbar (44) is a solid steel rod whose one end is welded to the center of the outer surface of the left arm of the horizontal bracket (53), and the other end is free. The cross section of the drawbar (44) is rectangular, and the length of the rectangle is 5-10 cm and the width is 4-6 cm; the drawbar insertion hole (43) is a cylindrical hole, which is arranged at the free end of the drawbar (44), The drawbar jack (43) has a circular cylindrical cross-section with a diameter of 3-5 centimeters and a height of 4-6 centimeters; the main power cable (12) is a double-strand copper-core power cable with a circular cross-section of the copper core. The diameter of the copper core of the power cord (12) is 3-8 mm; the main power cord plug (13) is a three-phase plug and is arranged at the free end of the main power cord (12). 4.根据权利要求1所述的利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，其特征在于：所述的加液泵(3)是利用电动水泵将水从接料冲斗(35)抽吸到反应罐(4)里为秸秆的腐熟分解提供水的水泵，由总电源线(12)供应电能，安装在水平支架(53)上，加液泵(3)包括加液管(8)和吸液管(16)；加液管(8)是加液泵(3)上部的水管，一端连通加液泵(3)泵体，另一端游离，开口在反应罐(4)顶部的罐顶进料口(33)处，中部通过固定环垂直方向固定在反应罐(4)上部外表面，加液管(8)为橡胶质，壁厚0.5-1厘米，壁内镶嵌着螺旋状的钢丝，钢丝横截面为圆形，圆形的直径为2-5毫米，加液管(8)内腔管径为5-10厘米；吸液管(16)是在加液泵(3)泵体的抽吸下将水从接料冲斗(35)抽吸出来的管道，吸液管(16)为橡胶质，壁厚0.5-1厘米，壁内镶嵌着螺旋状的钢丝，钢丝横截面为圆形，圆形的直径为2-5毫米，吸液管(16)内腔管径为5-10厘米，吸液管(16)一端连通加液泵(3)泵体，另一端伸到接料冲斗(35)底部，吸液管(16)在接料冲斗(35)底部这一端具有水龙头。4. the method for utilizing high cellulolytic active bacteria to quickly replenish the required organic matter in the process of remediation of saline-alkali wetlands according to claim 1, is characterized in that: described liquid adding pump (3) is to utilize electric water pump to remove water from The feeding hopper (35) is pumped into the reaction tank (4) to provide water for the decomposing and decomposing of the straw, and the main power line (12) supplies electric energy, and is installed on the horizontal support (53), and the liquid adding pump (3) ) includes a liquid addition pipe (8) and a liquid suction pipe (16); the liquid addition pipe (8) is a water pipe on the upper part of the liquid addition pump (3), one end is connected to the pump body of the liquid addition pump (3), the other end is free, and the opening is At the tank top feeding port (33) at the top of the reaction tank (4), the middle part is fixed on the outer surface of the upper part of the reaction tank (4) in a vertical direction through a fixing ring, and the liquid feeding pipe (8) is made of rubber, and the wall thickness is 0.5-1 cm , the wall is inlaid with a spiral steel wire, the cross section of the steel wire is circular, the diameter of the circle is 2-5 mm, the inner diameter of the liquid filling pipe (8) is 5-10 cm; the suction pipe (16) is The pipe that sucks water out of the receiving hopper (35) under the suction of the liquid feeding pump (3), the suction pipe (16) is rubber, the wall thickness is 0.5-1 cm, and the wall is inlaid with Spiral steel wire, the cross section of the steel wire is circular, the diameter of the circle is 2-5 mm, the inner diameter of the suction pipe (16) is 5-10 cm, and one end of the suction pipe (16) is connected to the liquid adding pump ( 3) The pump body, the other end extends to the bottom of the material receiving hopper (35), and the suction pipe (16) has a faucet at the bottom of the material receiving hopper (35). 5.根据权利要求1所述的利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，其特征在于：所述的抽水泵(10)是利用电动水泵将水从沟渠等水源内抽吸到接料冲斗(35)里、为反应罐(4)和冲刷从反应罐(4)下部的碎料机(1)里面出来的有机质液体和一些秸秆碎用水的水泵，由总电源线(12)供应电能，安装在水平支架(53)上，抽水泵(10)包括吸水管(11)、喷水管(14)；喷水管(14)是抽水泵(10)上部的水管，一端连通抽水泵(10)泵体，另一端游离，开口在接料冲斗(35)封堵壁处，中部横架在水平支架(53)和接料冲斗(35)之间，喷水管(14)为钢管，壁厚0.5-1厘米，内腔管径为5-10厘米；吸水管(11)是在抽水泵(10)泵体的抽吸下将水从沟渠等水源内抽吸到接料冲斗(35)里的管道，吸水管(11)为橡胶质，壁厚0.5-1厘米，吸水管(11)壁内镶嵌着螺旋状的钢丝，钢丝横截面为圆形，钢丝圆形的直径为2-5毫米，吸水管(11)内腔管径为5-10厘米，吸水管(11)的一端连通加液泵(3)泵体，另一端伸到沟渠等水源内，吸水管(11)在沟渠等水源内这一端具有水龙头。5. the method for utilizing high cellulolytic active bacteria to quickly replenish the required organic matter in the saline-alkali wetland repair process according to claim 1, is characterized in that: described pumping pump (10) is to utilize electric water pump to remove water from the ditch Wait for the water source to be pumped into the receiving hopper (35), for the reaction tank (4) and the water pump for washing the organic liquid and some straw crushing water from the crusher (1) at the lower part of the reaction tank (4), Electric power is supplied from the main power line (12), installed on the horizontal support (53), and the water pump (10) includes a suction pipe (11) and a water spray pipe (14); the water spray pipe (14) is a suction pump (10) The upper water pipe, one end is connected to the pump body of the suction pump (10), the other end is free, the opening is at the sealing wall of the receiving hopper (35), and the middle horizontal frame is between the horizontal bracket (53) and the receiving hopper (35). In between, the water spray pipe (14) is a steel pipe, the wall thickness is 0.5-1 cm, and the inner cavity diameter is 5-10 cm; The pipe that is sucked from the water source to the receiving hopper (35), the suction pipe (11) is made of rubber, the wall thickness is 0.5-1 cm, the wall of the suction pipe (11) is inlaid with spiral steel wire, and the cross section of the steel wire is The diameter of the circular wire is 2-5 mm, the inner diameter of the suction pipe (11) is 5-10 cm, and one end of the suction pipe (11) is connected to the pump body of the liquid filling pump (3), and the other end extends To the water source such as the ditch, the water suction pipe (11) has a tap at the end in the water source such as the ditch. 6.根据权利要求1所述的利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，其特征在于：所述的粉碎机(41)内有绞碎辊，粉碎机(41)基部呈长方体形，粉碎机(41)基部长方体形的长度为2-4米、宽度为1-1.5米、高度为0.5-1米，粉碎机(41)基部长方体下部设置4个滚轮，以便移动整个粉碎机(41)，粉碎机(41)在电机的带动下，绞碎辊将从粉碎机进料口(38)进来的秸秆粉碎；粉碎机(41)内还有鼓风结构；粉碎机进料口(38)是方形开口，各类秸秆在此处被塞入粉碎机(41)内；粉碎机出料嘴(37)是粉碎机(41)上部相对粉碎机进料口(38)一侧的扁管形结构，粉碎机出料嘴(37)基部口大，呈长方形，长方形的长度为1-1.5米、宽度为10-30厘米，粉碎机出料嘴(37)游离端开口小，呈椭圆形，椭圆形的长直径为10-30厘米、短直径为10-15厘米，粉碎机出料嘴(37)开口位于传送带(40)上面。6. the method for utilizing high cellulolytic active bacteria to quickly replenish the required organic matter in the process of repairing saline-alkali wetlands according to claim 1, is characterized in that: described pulverizer (41) has a crushing roller, and the pulverizer (41) The base is in the shape of a cuboid, the length of the cuboid shape of the pulverizer (41) is 2-4 meters, the width is 1-1.5 meters, and the height is 0.5-1 meters, and four rollers are arranged at the lower part of the cuboid of the pulverizer (41). , in order to move the whole pulverizer (41), the pulverizer (41) is driven by the motor, the pulverizing roller will pulverize the straw coming in from the pulverizer feeding port (38); the pulverizer (41) also has a blast structure The feeding port (38) of the pulverizer is a square opening, where all kinds of straws are stuffed into the pulverizer (41); (38) The flat tube-shaped structure on one side, the pulverizer discharge nozzle (37) has a large base and a rectangular shape, the length of the rectangle is 1-1.5 meters, and the width is 10-30 cm. The pulverizer discharge nozzle (37) The opening of the free end is small and oval, the long diameter of the oval is 10-30 cm and the short diameter is 10-15 cm, and the opening of the discharge nozzle (37) of the pulverizer is located on the conveyor belt (40). 7.根据权利要求1所述的利用高纤维素分解活性菌快速补充盐碱湿地修复过程中所需有机质的方法，其特征在于：所述的传送带(40)由传送带出料筒(34)、传送带围筒(36)、传送带接料平台(39)、传动带支杆(42)组成，传送带出料筒(34)是传送带(40)顶部的弯筒，传送带出料筒(34)筒壁为钢质，厚度为1-5毫米；传送带出料筒(34)基部连通传送带围筒(36)，端部游离，开口在罐顶进料口(33)的上方；传送带围筒(36)位于传送带出料筒(34)和传送带接料平台(39)之间，呈圆筒形，圆筒的直径为30-50厘米，传送带围筒(36)筒壁为钢质，厚度为1-5毫米，传送带围筒(36)内部设置有能够来回转动的皮带；传动带支杆(42)为钢质，横截面呈圆形，传动带支杆(42)的直径为3-10厘米、高度为0.3-0.5米；传送带接料平台(39)为水平设置，下部具有4个滚轮，传送带接料平台(39)上部设置有水平的皮带。7. the method for utilizing high cellulolytic active bacteria to quickly replenish the required organic matter in the process of repairing saline-alkali wetlands according to claim 1, is characterized in that: the conveyor belt (40) is discharged from the conveyor belt barrel (34), The conveyor belt perimeter (36), the conveyor belt receiving platform (39), and the transmission belt support rod (42) are composed. The conveyor belt discharge cylinder (34) is a curved cylinder at the top of the conveyor belt (40). Steel, with a thickness of 1-5 mm; the base of the conveyor belt discharge cylinder (34) is connected to the conveyor belt shroud (36), the end is free, and the opening is above the tank top inlet (33); the conveyor belt shroud (36) is located at The space between the conveyor belt discharge cylinder (34) and the conveyor belt receiving platform (39) is cylindrical, the diameter of the cylinder is 30-50 cm, and the conveyor belt surrounding cylinder (36) has a steel wall and a thickness of 1-5 cm. mm, a belt that can be rotated back and forth is provided inside the conveyor belt perimeter (36); the transmission belt support rod (42) is made of steel, the cross section is circular, and the transmission belt support rod (42) has a diameter of 3-10 cm and a height of 0.3 cm. -0.5 meters; the conveyor belt material receiving platform (39) is set horizontally, the lower part has 4 rollers, and the upper part of the conveyor belt material receiving platform (39) is provided with a horizontal belt.
CN202111541558.7A 2021-12-16 2021-12-16 Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria Active CN114208433B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202111541558.7A CN114208433B (en) 2021-12-16 2021-12-16 Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202111541558.7A CN114208433B (en) 2021-12-16 2021-12-16 Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria

Publications (2)

Publication Number Publication Date
CN114208433A true CN114208433A (en) 2022-03-22
CN114208433B CN114208433B (en) 2023-03-21

Family

ID=80702896

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202111541558.7A Active CN114208433B (en) 2021-12-16 2021-12-16 Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria

Country Status (1)

Country Link
CN (1) CN114208433B (en)

Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1101658A (en) * 1993-10-14 1995-04-19 王惠新 Method for producing biological soil amendment
CN105082395A (en) * 2014-05-16 2015-11-25 天津纳祥科技有限公司 Plastic product extrusion granulation machine
CN107988050A (en) * 2017-12-13 2018-05-04 魏传喆 A kind of high production natural pond device of biomass utilization rate
CN108704707A (en) * 2018-05-29 2018-10-26 霍邱金木鱼农业科技有限公司 A kind of biological organic fertilizer raw mill plant of good crushing effect
CN109265217A (en) * 2018-11-12 2019-01-25 南京评宇环境工程研究院（有限合伙） A kind of production method of soil conditioner
CN208643663U (en) * 2018-07-14 2019-03-26 绍兴丰飞环境建设有限公司 A kind of urban landscaping soil restoring device
CN212018058U (en) * 2020-03-19 2020-11-27 中国环境科学研究院 An environmental protection device for soil remediation
CN112094653A (en) * 2020-10-01 2020-12-18 长春黄金研究院有限公司 Improvement of Suda saline-alkali soil and generation method of biochemical fulvic acid raw material
CN213266336U (en) * 2020-08-13 2021-05-25 明洋(山东)环境科技有限公司 Fertilizer granule granulation equipment
CN113016288A (en) * 2019-12-09 2021-06-25 杨兰 A spout kind of equipment for hillock vegetation resumes
CN213880900U (en) * 2020-10-16 2021-08-06 王莹洁 Gardens are with quick fertilizer injection unit

Patent Citations (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1101658A (en) * 1993-10-14 1995-04-19 王惠新 Method for producing biological soil amendment
CN105082395A (en) * 2014-05-16 2015-11-25 天津纳祥科技有限公司 Plastic product extrusion granulation machine
CN107988050A (en) * 2017-12-13 2018-05-04 魏传喆 A kind of high production natural pond device of biomass utilization rate
CN108704707A (en) * 2018-05-29 2018-10-26 霍邱金木鱼农业科技有限公司 A kind of biological organic fertilizer raw mill plant of good crushing effect
CN208643663U (en) * 2018-07-14 2019-03-26 绍兴丰飞环境建设有限公司 A kind of urban landscaping soil restoring device
CN109265217A (en) * 2018-11-12 2019-01-25 南京评宇环境工程研究院（有限合伙） A kind of production method of soil conditioner
CN113016288A (en) * 2019-12-09 2021-06-25 杨兰 A spout kind of equipment for hillock vegetation resumes
CN212018058U (en) * 2020-03-19 2020-11-27 中国环境科学研究院 An environmental protection device for soil remediation
CN213266336U (en) * 2020-08-13 2021-05-25 明洋(山东)环境科技有限公司 Fertilizer granule granulation equipment
CN112094653A (en) * 2020-10-01 2020-12-18 长春黄金研究院有限公司 Improvement of Suda saline-alkali soil and generation method of biochemical fulvic acid raw material
CN213880900U (en) * 2020-10-16 2021-08-06 王莹洁 Gardens are with quick fertilizer injection unit

Also Published As

Publication number Publication date
CN114208433B (en) 2023-03-21

Similar Documents

Publication Publication Date Title
CN109454108B (en) Microbial remediation equipment and remediation method for heavy metal polluted soil
CN107567733A (en) A kind of miniature hand pulling type soil remediation device
CN213548313U (en) Agricultural fertilizing and seeding device
CN212278760U (en) Agricultural equipment for improving soil in agriculture
CN108480386A (en) A farmland pollution control device for treating surface pollution
CN216460840U (en) Be used for prosthetic equipment of heavy metal cadmium soil
CN117564075A (en) An ecological protection forest soil restoration device
CN112126585A (en) Microbial fermentation pretreatment device for returning rice straws to field
CN112889456A (en) Cassava stem cutting and returning all-in-one machine
CN107999526A (en) A kind of full-automatic integral formula chemical oxidation and solidification and stabilization soil remediation equipment
CN208437421U (en) A kind of farming soil remediation processing unit
CN114208433B (en) Method for rapidly supplementing organic matters required in saline-alkali wetland restoration process by using high-cellulose decomposition active bacteria
CN119278842B (en) A water-saving irrigation device for fruit trees
CN105830566B (en) Multifunctional soil oxygenation sterilization residual pesticide removing farming machine
CN204408867U (en) Multifunction soil oxygenation sterilization is removed remains of pesticide and is cultivated machine
CN211792765U (en) Agricultural soil pH value restores and uses device
CN107931324A (en) A kind of novel intelligent soil restoring device
CN111567171A (en) A device for saline-alkali soil improvement
CN209969187U (en) Efficient labor-saving integrated soil remediation device
CN209806375U (en) Soil treatment is buried and mixed integrative structure with modifier
CN209602336U (en) A kind of dedicated sewage-treatment plant of animal epidemic prevention
CN217790330U (en) A citrus water and fertilizer integrated irrigation and fertilization device
CN217905043U (en) Agricultural equipment for improving soil
CN212018919U (en) Soil prosthetic devices is used to agricultural
CN114505336A (en) Ecological restoration auxiliary device for heavy metal region and application method thereof

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
GR01 Patent grant
GR01 Patent grant