WO2023232087A1

WO2023232087A1 - Clean product set prepared by using energy grass as raw material, and preparation method therefor

Info

Publication number: WO2023232087A1
Application number: PCT/CN2023/097506
Authority: WO
Inventors: 唐禹豪; 陈汇宏; 胡嘉庆; 唐宏玮; 沙良宝
Original assignee: 唐禹豪; 陈汇宏; 胡嘉庆
Priority date: 2021-06-04
Filing date: 2023-05-31
Publication date: 2023-12-07
Also published as: CN115431429A; CN115433472A; CN115431431A; CN115431430A

Abstract

Provided in the present invention are a clean product set prepared by using energy grass as a raw material, and a preparation method therefor. The "product set" is characterized in that energy grass, or energy grass and cow dung are used as starting main raw materials, processing sub-paths are connected in series or parallel for integration into a process and a combined apparatus or device array for clean production, and ultimately a clean product set is prepared. The "product set" is specifically composed of a main product A, or a combination of the main product A and any one or two of by-products B and C, or a combination of the main product A, the by-product B/C and any one or more of auxiliary products D, E, F, G, H and I, wherein A is hydrophilic de-fibered fibers, B is coarse grains of wood-plastic composite regenerated substances, C is a lignin/resin mixture, D is a solid organic soil conditioner, E is a liquid organic soil conditioner, F is fermented feed, G is pellet feed, H is a biomass pellet fuel, and I is edible fungus planting rods/blocks.

Description

Collection and preparation methods of cleaning products using energy grass as raw materials

Technical field

The present invention provides a collection of cleaning products and a manufacturing method using energy grass as raw materials, which involves classifying some grain, cotton, oil and other crops that produce huge amounts of straw or branches into the high-level name of energy grass, and then They all use energy grass as the upper name, and introduce the process of integrating clean production in series and parallel through processing sub-paths and combined equipment or device array using it as the main raw material, and finally produce a collection of clean products, which belong to straw and giant fungus grass. The technical field of comprehensive utilization of grasses, etc.

Background technique

According to the explanation of the online Baidu Encyclopedia: Energy grass is not the name of a plant grass. Tall perennial herbs or semi-shrubs, including sweet sorghum, switchgrass, Miscanthus crops and other tall herbs can be labeled as energy grasses; energy grasses are mostly resistant to drought, salt and alkali, barrenness and adaptability. Grass seeds are simple to plant and manage, and can be planted in arid and semi-arid areas, low-lying areas prone to waterlogging and saline-alkali areas, mountainous areas with poor soil, and semi-mountainous areas; energy grass does not have high requirements for soil quality and climate, and is cold-resistant, frost-resistant, and adaptable. It is strong, fast growing and has high yield. The maximum annual hay output per mu of farmland can reach more than three tons. After one sowing, the grass production period can be as long as 10 to 15 years.

Counting from October 19, 2021, the day when this application was started to be written, the total number of inventions and utility models obtained by entering the word "energy grass" from the "soopat official website" of the Chinese patent website is only less than a hundred. 81 items; that is, at least in our country, there are not many patent applications with energy grass as the upper name.

From the aforementioned explanation on Baidu Encyclopedia, we can know that energy grass has the characteristics of "low requirements on soil quality and climate, cold and frost resistance, strong adaptability, fast growth and high yield". However, there is no literature report on how this characteristic can be applied to energy grass for water purification and other purposes in subsequent uses.

In the use of energy grass, how can we not produce pollution, but also absorb pollution in the social environment such as cow dung, waste plastics, etc., or how to use the generated washing and other wastewater in the subsequent use of energy grass. There is no systematic report in the literature on the green utilization of resources.

Therefore, after preliminary understanding, the inventor believes that the deep processing and comprehensive utilization of energy grass can at least provide some product collections and clean production methods that are more beneficial to large-scale, raw material and convenient downstream motorization applications. This is the energy grass. Comprehensive utilization required in this field.

In addition, today's grain, cotton, oil and other crops will produce a huge amount of straw waste after harvesting. One of the current mainstream applications is to make biomass pellet fuel for energy use, so these straw wastes are used There is nothing wrong with classifying crops that produce a large amount of straw under the high-level name of energy grass.

Furthermore, from the aforementioned semi-shrubs, they can be named as energy grasses, and from the online Baidu entry of semi-shrubs, the explanation is: "The difference between semi-shrubs and shrubs is that only the lower parts of the branches are perennial and have corks. Tissue protection, the upper parts are 1-year-old. Therefore, in the cold winter, the upper branches wither or die, and are often cut down by farmers for firewood." The inventor explained that artificial dwarf planting will be expanded and planted every year. Willow trees, bamboo willows, poplar trees, mulberry trees, medlar trees, etc. whose upper branches need to be pruned are also classified under the upper name of energy grass.

Contents of the invention

The purpose of the present invention is to provide a collection and preparation method of cleaning products using energy grass as raw materials in view of the current situation that the existing application technology for energy grass may be few or insufficient. The main product A in the "product set" is hydrophilic and decomposable fiber, whose physical properties can at least replace or partially replace traditional recycled pulp, which is used as a raw material for papermaking or further processing to make bleached pulp, etc.; by-products, One is the wood-plastic composite recycled coarse particle product B, or/and the other is the lignin/resin mixture product C; moreover, it can also include a group of auxiliary products D, E, F, G, H, and I. In the "product collection", the main product is surrounded by by-products or/and auxiliary products, and all the by-products produced in the preparation of the main product are squeezed out. Finally, for all The products, manufacturing methods, equipment, etc. provided also provide their specific directional uses.

The idea of the present invention is to provide a set of products and a clean manufacturing method that are convenient for large-scale, raw material and downstream motorized applications. The above-mentioned "clean production method" not only needs to clean up the snow in front of the house, but also greenly utilize all resources such as waste liquid produced during the comprehensive utilization of energy grass; it must also take away the frost on other people's tiles, which is not only for Wastes such as cow dung around the implementation site or discarded agricultural mulch films in the fields are also absorbed and used for green utilization of resources. Of course, the invention also borrows the high-level name of energy grass to convert some grain, cotton, oil, etc. containing straw Or crops with huge branches are also classified among them, in the hope that the technical solution of the present invention can be applied to more herbaceous or artificial dwarf tree species whose upper branches need to be pruned every year; in the preparation of the main product A In terms of the use of hydrophilic fiber-dissolving additives, the traditional material collection of "any or multiple combinations of caustic alkali, ammonia, ammonium salts, peroxides, biological enzymes, etc." is replaced by a small amount of whiskers, etc. Additives are a new way to achieve roughening modification such as surface grafting/coating of fibers, roughening the surface of fibers and making them in water, which can achieve the purpose of collision between fibers or combining with winding to form paper. Finally, some specific or extended uses of the products and preparation methods described in the present invention are provided.

The idea of the present invention is to achieve the above objects through the following technical solutions:

1. A collection of clean products using energy grass as raw material, which is characterized by: using energy grass, or energy grass and cow dung as the starting main raw materials, the series and parallel integration of clean production processes and combined equipment or device arrays through processing sub-paths , and finally a cleaning product set is obtained. The "product set" is specifically composed of the main product A as described below, or a combination of the main product A and any one or two of the by-products B and C; or the main product A or by-product B/C, and a combination of any one or more of auxiliary products D, E, F, G, H, and I:

The main product A _- hydrophilic decomposable fiber, characterized by: using the aforementioned "energy grass, or energy grass and cow dung", crushed by any one or more combinations of sawing/milling/cutting/hammering and then sieving to obtain the "Elongated fiber bundles of any mesh size that pass through a sieve ranging from 3 mesh to no more than 28 mesh" are used as raw materials; the brown/black liquor will be discharged during the preparation process, and the "brown/black liquor" will be discharged. The ratio of the weight part W _{brown/black liquor} of "black liquor" to the weight part W _A of the absolute dry fiber containing no more than 15% water in the main product A is W _{brown/black liquor} /W _A = 90~100~300 /100 range; and the ratio of the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained in the "brown/black liquor" to the liter volume of the water contained is ≤0.034mol/L, and its pH value is within 5.0~9.4 range; the total content of any one or more of caustic alkali, ammonia, ammonium salts, peroxides, and biological enzymes in the additives used is 0; or the water-insoluble or poorly soluble substances used in the preparation To make a whisker additive, implement low-ash whisker grafting/coating on the fiber surface. The "whisker additive" added to 100 parts by weight of the absolutely dry fiber in the main product A is ≤ 1 to 3 ~5~9 parts by weight, either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight; the main product A - a hydrophilic and decomposable fiber product, cannot be dissolved after being put into water or stirred again. floating surface;

The main product A can be subdivided into the main product A-1--a hydrophilic decomposable fiber controlled to have a low hydrophilicity of beating degree <16°SR, and the main product A-2--controlled to be Hydrophilic and decomposable fiber with high hydrophilic beating degree ≥16°SR;

By-product B - wood-plastic composite regenerated coarse particles; characterized by: at least the above-mentioned "energy grass" is crushed by any one or more combinations of sawing/milling/cutting/hammering, and then screened. The other part: "Fine materials or/and crushed materials that pass through a 28-mesh sieve, or crushed materials that are mixed with coarse and fine materials that pass through a 3-mesh sieve", and then use them as raw materials together with "waste plastics", or mix them with those in A The "brown/black liquor" has a mass transfer connection and is pelletized using a biomass fuel pellet machine;

By-product C - lignin/resin mixture, characterized by: It is produced using the "brown/black liquor" mentioned in A as raw material. It is a hydrophilic liquid in the color of black brown at room temperature, or in the form of a paste-like brown or Nearly black colloid, or in the form of coffee or nearly black powder or granules, or in the form of rosin-like solid; the by-product C, which can be subdivided into by-product C-1-edible or medical grade lignin/resin mixture, By-product C-2--feed or industrial grade lignin/resin mixture;

Auxiliary product D - solid organic soil conditioner, characterized by: the remaining material after extracting "energy grass, or energy grass and cow dung" that does not pass the 28-mesh sieve to make the main product A. Energy grass powder or fine cow dung sediment, As one of the ingredients in solid organic soil amendment;

Auxiliary product E - liquid organic soil conditioner, characterized by: utilizing the brown/black liquor discharged during the preparation of the hydrophilic decomposable fiber main product A, or/and utilizing the discharged liquid due to the upgrading of the main product A and by-product C Pressed liquid or/and washing liquid or/and elutriated liquid, products blended according to the soil requirements of the crops and fields to be applied; the "discharged pressed liquid or/and washing liquid or/and elutriated liquid" Or "brown/black liquor", with a pH value in the range of 5.0 to 9.4, and the ratio of the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained in it to the liter volume of the water contained therein is ≤0.034 mol /L, or the total wt% concentration of the soluble sodium salt, potassium salt, and magnesium salt contained therein is ≤ 0.20% (wt%), or the total concentration of the soluble sodium salt, potassium salt, and magnesium salt contained therein is consistent with the production implementation The difference in the total concentration of soluble sodium salts, potassium salts, and magnesium salts in the water source taken from the local area is ≤0.01% (wt%); the weight ratio of auxiliary product E and main product A is controlled at W _E /W _A ≤500/ 100, or ≤ or 2000/100 ≤ or 3000/100 range;

Auxiliary product F - fermented feed, characterized by: the product is mixed with the "brown/black liquor" discharged during the preparation process of main product A;

Auxiliary product G - pellet feed, characterized by: the energy grass dry material is only crushed and sieved to obtain a fine powder that passes through a 28 mesh sieve, or/and a particle size with a small soil content that passes through a 28 to less than 150 mesh sieve. The energy grass fiber powder in the center is used as one of the ingredients of pellet feed;

Auxiliary product H - biomass pellet fuel, characterized by: the fine powder obtained by crushing and sieving the energy grass to remove the crude fiber that has not passed the 28 mesh sieve, or the full-component crushed energy grass as ingredients. components, or waste plastics are added; the "waste plastics" include at least any one or combination of waste agricultural plastic films, waste foam plastics, waste chemical fiber fabrics or/and chemical fiber cotton batting, and the "waste plastics" "Additional" accounts for less than 5% of the total weight of auxiliary product H, or does not exceed 22%;

Auxiliary product I - Edible fungus planting stick/block, characterized by: the remaining material after extracting the main product A from "energy grass, or energy grass and cow dung" with a mesh size of no more than 28 mesh, and passing through a 28 mesh sieve. The energy grass powder or fine cow dung sediment of the hole is used as one of the ingredients in the edible fungus planting sticks/blocks.

2. The "main product A--hydrophilic and decomposable fiber" described in technical solution 1, its characteristics include at least the following ⅰ to ⅵ, or a combination with ⅶ:

ⅰ. Raw materials used: including Echinacea, Liba, lemongrass, Arundodis, reeds, reeds, zebra grass, elephant grass, king grass, king bamboo grass, giant fungus grass, five-jointed miscanthus, rice grass, purple elephant grass , dwarf elephant grass, red elephant grass, sweet elephant grass, grass shoots, grass sugarcane, pseudosorghum, sweet sorghum, Peter grass, Sudan grass, Taiwan sweet grass, Pennisetum alterniflora, Spartina alterniflora hybrid, American wolftail Energy grasses of any one or more combinations of grasses and hybrid pennisetum, grain, cotton, and oil crops that produce a large amount of straw - rice, wheat, corn, cotton, rape, soybean, oil peony, oil peony, sunflower, Energy grass of any one or more combinations of castor straws, or any one or more combinations of willows, bamboo willows, poplars, mulberry trees, and wolfberry trees that are artificially planted in dwarfs and whose upper branches need to be pruned all year round. Grass; crushed by any one or more combinations of sawing/grinding/cutting/hammering and then sieved, a part of it is obtained: fine particles with any mesh size ranging from 3 mesh to no more than 28 mesh sieve or mixed particle size Fragments of long fiber bundles;

ⅱ. By-product materials: By-product material 1: Brown/black liquor discharged from the hot water delignification/resin process. When making the "A" mentioned above, dry materials will be used in the hot water delignification/resin process. , the brown/black liquor is discharged by pressing/squeezing; the "brown/black liquor" has a weight part W of _{the brown/black liquor} and a weight part W of the absolute dry fiber containing no more than 15% water in the main product A obtained The ratio of _A is in the range of W _{brown/black liquor} /W _A =90~100~300/100; the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained in the "brown/black liquor" are equal to The volume ratio per liter is ≤0.034mol/L, or/and the total wt% concentration of the soluble inorganic sodium salts, potassium salts, and magnesium salts contained in the water is ≤0.20% (wt%), or the soluble inorganic salts and potassium salts contained in the water The difference between the total wt% concentration of salt and magnesium salt and the total concentration in the water source taken from the production site is ≤0.01% (wt%), and the pH value of the "brown/black liquor" is in the range of 5.0 to 9.4;

Or by-product material 2: fresh juice obtained from fresh energy grass or fresh energy grass washed with water and then squeezed; or juice obtained from dried energy grass washed with water and then boiled and squeezed;

Or and by-product material 3: using cow dung as the starting material, the washing/washing liquid discharged after washing/washing the cow dung;

Or and by-product material 4: Use activated carbon and acidic clay to adsorb, decolorize and purify the aforementioned "brown/black liquor". The decolorized adsorption sludge obtained after purifying circulating water; or the aforementioned "brown/black liquor", obtained by adding sulfuric acid dropwise to acidify it until the pH value does not exceed 7.0, and using activated carbon or activated carbon and acidic clay to purify circulating water. Decolorization and adsorption of sludge;

Or and by-product material 5: decolorized precipitated sludge obtained by precipitation and purification of the aforementioned "brown/black liquor" or/and "washing liquor" using chemical or biochemical methods;

ⅲ. Residual color: Add the main product A into clean water, heat the product to 70°C and bubble it for 5 to 10 minutes, then squeeze out the clear liquid material that has not evaporated and lost weight. The color of the color tube intuitively or the colorimeter detects is not thicker than the color of the "brown/black liquid" mentioned in item ⅱ diluted 16 times with clean water, or the instrument detects that its COD or BOD value is not higher than the "brown/black liquor" mentioned in item ⅱ The COD or BOD value of the "black liquor" diluted 16 times by the volume of clean water, or the discoloration consumption value of potassium permanganate measured by volumetric titration is not higher than the value of the "brown/black liquor" diluted 16 times by the volume of clean water as described in item ⅱ Potassium permanganate fading consumption value;

ⅳ. Product dosage form: The dosage form of the main product A can be a loose meat floss-like moist material with a water content of not more than 75%, a wet paper-like material with a water content of not more than 75%, a dry meat floss-like material with a water content of not more than 20%, and a water-based material. Any of paper-like dry materials containing no more than 20% water, compacted brick-shaped dry materials containing no more than 20% water, and compacted granular dry materials containing no more than 20% water;

ⅴ. Physical properties: Main product A-1 controlled to have a low hydrophilicity with a beating degree of <16°SR, or A-1 and main product A-2, A controlled to have a high hydrophilicity with a beating degree of ≥16°SR. -1 and A-2 are two sets of materials that can be blended easily and arbitrarily; when compared with the standard sample dough - the feces of beetle larvae or wood beetle moth larvae eating willow stems, the dough is compared with the dough. In the pinch test of the material, the hardness of A-1 or A-2 ≤ the hardness of the standard sample; or in the test of rubbing the dough with the standard sample for at least 10 times, it can be seen with the naked eye or Use a balance to weigh and compare, the amount of scattered chips of A-1 or A-2 is not more than 5 times the amount of scattered chips of the standard sample;

ⅵ. Production process characteristics: During the production process, the ratio of the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained in the water involved to the liter volume of "water" is ≤0.034 mol/L; and adopt Impregnate the fiber material with water of not less than 70°C at least twice to remove the lignin/resin in the fiber; the flow direction of the gradually thickening brown/black liquor in the "water" flow is consistent with the flow direction of the fiber material in the production process The flow direction in the product is countercurrent; or water-insoluble or poorly soluble substances are added as whisker additives, and the amount added is ≤1~3~5~9 parts by weight for 100 parts by weight of absolute dry fiber in the main product A or its intermediate product parts by weight, either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight, implement low-ash whisker grafting/coating on the fiber surface; among the additives used, caustic alkali, ammonia The total content of any one or more of ammonium salts, peroxides, and biological enzymes is 0;

ⅶ. Preferable parameters: or "The ratio of the discharged weight part W _{brown/black liquor} and the total obtained weight part W _A of the absolutely dry main product A with a water content not exceeding 15% as described in item ⅱ is W _{brown/black Liquid} /W _A = 100~120~150/100 range; or "adding water-insoluble or poorly soluble substances as whisker additives as described in item ⅵ, the amount added is equivalent to the absolute dry fiber in the main product A or its intermediate product "100 parts by weight""is ≤1~3~5 parts by weight", "either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight"; the "whisker additive" is at least a saturated aqueous solution of calcium hydroxide , any of silica sol, etc., or/and newly generated calcium hydroxide, aluminum hydroxide, hydrated silicic acid, calcium silicate, magnesium silicate, aluminum silicate, calcium carbonate, and calcium sulfate dihydrate in the aqueous phase , iron hydroxide, etc., or any combination of kaolin, clay, fly ash, wollastonite, etc. that has been ultrafinely pulverized to the point where it is difficult to naturally precipitate in water to a clear surface within half an hour. Or a combination of more, or a combination of any one or more of kaolin, clay, fly ash, wollastonite, etc. crushed to 320 mesh.

3. The "by-product B - wood-plastic composite regenerated coarse particles" described in technical solution 1 is more characterized by: the characteristics of "wood" are the following 3-1 or the combination of 3-1 and 3-2, wherein The characteristics of "plastic" are the following 3-3 or the combination of 3-3 and 3-4, and the product dosage form characteristics are the following 3-5 to 3-8:

3-1. The “wood” includes part of the energy grass: fine materials or/and crushed materials that pass through a 28-mesh sieve, or crushed materials mixed with coarse and fine materials that pass through a 3-mesh sieve;

3-2. The "part" as described in 3-1 above is the dry basis weight of the "wood" containing 15% of equilibrium water after natural drying in the air, accounting for 5% to 5% of the total weight of by-product B. Between 78% (wt%);

3-3. The raw materials for "plastic" are all selected from waste plastics;

3-4. "Waste plastics" as described in 3-3 above, including at least any one or a combination of more as described below: waste paper recycling The discarded miscellaneous waste plastic film slag, including the floating plastic-containing materials or/and submerged plastic-containing materials obtained by water flotation of the "miscellaneous waste plastic film slag"; plastic film waste packaging bags and plastic film packaging of commodities Cut/punch edge materials in bag production, waste composite plastic film materials, plastic film composite release paper/film discarded in the production/use of trademark labels, waste aluminum-plastic composite film, waste agricultural plastic film; processed from waste tires Crushed and separated polymer fibers containing impurities, waste chemical fiber flannel removed from cars, waste chemical fiber carpets, waste chemical fiber fabrics, waste chemical fiber meltblown cloth, waste chemical fiber filter paper; waste wire plastic skins, waste plastic packaging tapes, waste Plastic woven bags, waste geotextiles, waste/old plastic shoes, waste plastic flooring products, waste plastic toys, waste plastic barrels, waste plastic bottles, waste plastic geotextiles, waste/old plastic lawns, waste plastic building materials, waste plastics Pipes, waste plastic boards, waste plastic stationery, waste plastic boxes/bags, waste plastic miscellaneous items; waste PVC artificial leather, waste PU artificial leather; waste foam plastics;

3-5. The dosage form of by-product B can be at least set into the first group of A, B, C, and D, or/and the second group of E, Ji, Geng, and Xin, or/and the third group of Ren and Gui. , that is, any one or more of A to Gui in the first to third groups can be blended and combined in any ratio to easily make the downstream plastic particles or coarse particles of wood-plastic composite regeneration. The total weight of "wood" or "wood" carrying "impurities" in the product ranges from 5% to 78%; the weight ratio of the two in the aforementioned "wood carrying 'impurities'" is W _impurities / W _wood = 0 ~ 10/100, the "wood" is an absolutely dry material with a moisture content of no more than 15%, and the "impurities" are "by-product materials 4" as described in ⅱ of the technical solution 2 ” or/and “by-product material 5”; the total weight input ratio of “plastic” and softener is in the range of 22% to 95%, and the weight ratio of the two in the aforementioned “plastic” and softener” is W _{waste Plastic} /W _softener =100/0～100:

First group:

The total weight input of "wood" in A includes 76%, and the total weight input of waste plastics and softeners accounts for 24%;

The total weight input of "wood" in B is 35%, and the total weight input of waste plastics and softeners is 65%;

The total weight input of "wood" in C is 25%, and the total weight input of waste plastics and softeners is 75%;

The total weight input of "wood" in D is 5, and the total weight input of waste plastics and softeners is 95%;

Second Group:

The total weight input of "wood" in E includes 77%, and the total weight input of waste plastics and softeners accounts for 23%;

The total weight input of "wood" accounts for 38%, and the total weight input of waste plastics and softeners accounts for 62%;

The update includes that the total weight input of "wood" accounts for 23%, and the total weight input of waste plastics and softeners accounts for 77%;

The total weight input of "wood" in Xin is 10, and the total weight input of waste plastics and softeners is 90%;

The third group:

The total weight input of "wood" in Renzhong accounts for 78%, and the total weight input of waste plastics and softeners accounts for 22%;

The total weight input of "wood" in Guizhong accounts for 15%, and the total weight input of waste plastics and softeners accounts for 85%;

3-6. Or as described in item 3-5, "select one or more of the A to Gui in the first to third groups and use them in combination to control the downstream coarse particles of the wood-plastic composite regenerated material. The total weight of "wood" in plastic particles or products is in the range of 5% to 78%, and the total weight of "plastic" and softener is in the range of 22% to 95%", items 3-5 The proportion of the total weight of "wood" in each feeding combination from A to Gui in the "first group", "second group" and "third group", and the proportion of the total weight of "plastic" and softener, All can be customized according to market customers;

3-7. The "wood-plastic composite recycled coarse particles" are composed of materials according to the "first group" or/and the "second group" or/and the "third group" mentioned in item 3-5. The ingredients from A to Gui are combined and fed. After being processed by a coarse granulator, the resulting texture is low-strength coarse granules that can be directly pulled/pulled/pinched/teared/grabbed with fingers/palms. The "low-strength coarse granules" "Strength", at least the standard sample specimen of plastic with tensile strength ≤3PMa;

3-8. The "coarse granulator" mentioned in item 3-7 above specifically refers to any feed pellet machine, organic fertilizer granulator, or biomass fuel pellet machine with continuous feeding/discharging function. , or a spiral granulator and intermediate crusher can be connected in series after the aforementioned "granulator"/"granulator".

4. The manufacturing method of "main product A--hydrophilic and decomposable fiber products" in the product set described in technical solution 1, and its characteristics May include the following steps one to ten:

Step 1 - Pretreatment and preparation of materials: First classify the energy grass dry materials, or further remove the metals or/and masonry blocks or/and bark impurities contained in the classified materials, and then The classified and impurity-free energy grass is then subjected to any one or more combinations of sawing/grinding/cutting/hammering, and then sieved; the crushed energy grass that passes through a 28-mesh sieve is discharged for further use;

Sieve out the elongated fiber bundles with classified or mixed particle sizes in any mesh range from 3 mesh to 28 mesh in the energy grass crushed material;

Or the slender fiber bundle energy grass crumbs that have been removed and purified are subjected to mechanical expansion processing;

Thus, the backup energy grass crumbs prepared for step 2 are obtained. This "backup energy grass crumbs" material is called natural absolutely dry material based on its naturally adsorbed equilibrium water content in the air of 15% (wt). ;

Step 2 - First batching: Take 100 parts by weight of the natural dry material of the "Standby Energy Grass Crushed Material" obtained in Step 1, and mix in the "Second Solid-Liquid Separation" described in the subsequent Step 7. The extruded water, the "stirring in" and "extruded water", after measuring the free content carried by 100 parts by weight of the natural bone-dry material in the solid phase obtained by the "first solid-liquid separation" described in the subsequent step 4 If the amount of water is Active agent: any one or combination of sodium butylnaphthalene sulfonate, sodium dodecylbenzene sulfonate, sodium lauryl sulfate, or/and coconut oil fatty acid diethanolamide, fatty alcohol polyoxyethylene Any one or a combination of multiple ethers; the "2x" corresponds to 100 parts by weight of the natural dry material of crushed energy grass materials: in the range of 25 to 50 to 300 parts by weight;

Step 3 - Heating and dissolution: Add the aforementioned "100 parts by weight of the natural dry material of the 'Standby Energy Grass Crushed Material' material" and "the extruded water obtained from the 'second solid-liquid separation' described in the subsequent step 7": "2x parts by weight", or "0.1 to 0.3% by weight of 'surfactant' of '2x parts by weight' of 'squeezed water'", place these materials in a tank that can be stirred, mixed, heated and kept warm. During the process, the material is uniformly stirred and heated to above 70°C, and kept warm for at least 5 minutes, or sampled and analyzed. When the color of the extruded liquid no longer changes to a darker color, the heating and heat preservation operations can be stopped;

Step 4 - The first solid-liquid separation: Introduce the material after the above "heating and heat preservation operations" into a screw or roller extruder, perform a mechanical kneading treatment on the fiber bundles of the material, and then knead it. The materials are introduced into a solid-liquid separator for solid/liquid separation; or the materials after the above-mentioned heating and heat preservation operations are directly introduced into a solid-liquid separator for solid/liquid separation; thereby obtaining the "pressed/extruded brown material" as described in technical solution 1. / black liquor", and the moisture material of the hydrophilic decomposed fiber intermediate product A to be treated, which has initially removed the water solute in the fiber;

In this "first solid-liquid separation", the "pressed/extruded brown/black liquor" obtained is naturally separated from the hydrophilic decomposable fiber intermediate product A by the weight portion of the _{discharged brown/black} liquor. The proportion of dry material weight part W _{hydrophilic decomposable fiber intermediate product A} can be controlled by using conventional solid-liquid separation machinery at W _{pressing/extrusion brown/black liquor} /W _{hydrophilic decomposable fiber intermediate product A} =25~100~ In the range of 300/100, in this "first solid-liquid separation", the weight percentage of the natural absolute dry material of the "hydrophilic and decomposable fiber intermediate product A" in the obtained moisture material can be controlled between 80% and 50%. 25% range;

Step 5 - Second batching: It is determined that the free water carried by 100 parts by weight of the natural dry material in the solid phase of the "moist material for the hydrophilic decomposable fiber intermediate product A" described in step 4 is x parts by weight. Then, take 100 parts by weight of the natural dry material contained in the "moist material of the hydrophilic decomposable fiber intermediate product A to be treated" and x parts by weight of free water, and then mix in the "third solidification step" described in the subsequent step ten. The extruded water obtained by "liquid separation" is not less than: Whisker auxiliary, the "whisker auxiliary" is at least any one of saturated aqueous calcium hydroxide solution, silica sol, etc., or/and newly generated calcium hydroxide, aluminum hydroxide, hydrated silicic acid in the aqueous phase , any one or a combination of calcium silicate, magnesium silicate, aluminum silicate, calcium carbonate, calcium sulfate dihydrate, ferric hydroxide, etc., or/and ultrafinely pulverized to the point where it cannot naturally dissolve in water within half an hour. Any one or combination of kaolin, clay, fly ash, wollastonite, etc. that has been precipitated until the surface water is clear, or kaolin, clay, fly ash, silica fume, etc. that are crushed to 320 mesh Any one or a combination of stones, etc.; the "whisker additive", the amount added to 100 parts by weight of absolute dry fiber in the "moist material of hydrophilic decomposable fiber intermediate product A" is ≤ 1 to 3 ~5~9 parts by weight, that is, the added amount is ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight;

Mix the second batching ingredients described in step 5 in the mixing tank first to form the materials to be processed by high-concentration grinding;

Step 6 - Grinding and latent elimination: Introduce the "materials to be processed into high-concentration grinding" obtained in step 5 into high-concentration grinding; or then use the heat to introduce the heat-generating materials from high-concentration grinding into a disinfection machine with heat preservation settings. Insulate or heat in a submersible tank, and let it stand at a temperature of no less than 70°C to relax the kinks and curls of the fibers produced during the high-concentration grinding process, and to dissolve the hydrophobic lipids in the fibers; After processing in step 6, the material after grinding or processing is obtained and is subject to solid-liquid separation;

Step 7 - The second solid-liquid separation: Introduce the above-mentioned "material after grinding or processing" into a screw or roller squeezer, and then perform mechanical kneading treatment on the fiber bundles of the material, and then Then the material is introduced into the solid-liquid separator for solid/liquid separation; or mechanical softening is omitted, and the above-mentioned "materials after grinding or processing" are directly introduced into the solid-liquid separator for solid/liquid separation; thus, we get As described in the previous "Step 2", "the extruded water obtained from the 'second solid-liquid separation'" and the wet material of the hydrophilic decomposable fiber intermediate product B to be treated are finally washed with new water;

Step 8 - The third batching: It is determined that the free water carried by 100 parts by weight of the natural dry material in the solid phase of the "moist material of the hydrophilic decomposable fiber intermediate product B to be treated" described in step 7 is x parts by weight. Then, take 100 parts by weight of the natural dry material contained in the "moist material to be processed for the hydrophilic decomposable fiber intermediate product B" and x parts by weight of free water, and then mix in new water or a small amount of recycled water for decolorization and impurities. In: Any of calcium hydroxide, aluminum hydroxide, silica sol, etc., or/and newly generated calcium hydroxide, aluminum hydroxide, hydrated silicic acid, calcium silicate, magnesium silicate, aluminum silicate in the water phase , any one or a combination of calcium carbonate, calcium sulfate dihydrate, ferric hydroxide, etc., or kaolin, clay, fly ash that has been ultrafinely pulverized to the point where it is difficult to naturally precipitate to a clear surface in water within half an hour. , any one or more combinations of wollastonite, etc., or any one or more combinations of kaolin, clay, fly ash, wollastonite, etc. crushed to over 320 mesh; the "whisker additive" , the added amount of 100 parts by weight of absolute dry fiber in the "moist material of hydrophilic decomposable fiber intermediate product B" is ≤1~3~5~9 parts by weight, that is, the added amount is ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight; add water and whisker additives according to the measurement in step eight to obtain the third batch of ingredients to be sent to step nine;

Step 9 - Stirring and washing: Introduce the "third batching" of the above step 8 into the screw or roller extruder, and then perform mechanical kneading treatment on the fiber bundles of the material, and then introduce the material to be finalized. The squeezed material is temporarily stored in a temporary storage tank; or the above-mentioned "third batching" is directly introduced into the mixer for stirring, so that the new water, or the moisture content of the solid-phase fiber mixed with the whisker additive and the hydrophilic decomposable fiber intermediate product B is The old water-containing material is fully mixed, and then the material is introduced into the temporary storage tank for the material to be finally squeezed dry; through the processing in step nine, the material to be sent to step ten to be finally squeezed dry is obtained;

Step 10 - The third solid-liquid separation or final modification: Introduce the "material to be finally squeezed dry" in the above-mentioned step 9 into the solid-liquid separator for solid/liquid separation; thus obtain the material as in the previous "step five" The above-mentioned "extrusion water obtained from the 'third solid-liquid separation'", and the final product - the hydrophilic and decomposable fiber A product including A-1 or/and A-2; or and then adding masking to the final product Iron/manganese ion additives: oxalic acid, sodium oxalate, potassium oxalate, ammonium oxalate, ethylenediaminetetraacetic acid, sodium ethylenediaminetetraacetate, tetraacetylethylenediamine, citric acid, sodium citrate, tartaric acid, sodium tartrate, A combination of any one or more of gluconic acid, diethylenetriaminepentaacetic acid, diethylenetriaminepentamethylenephosphonic acid, pentasodium diethylenetriaminepentacetate, and sodium nitrilotriacetate, so The above composition material can be formulated into a masking aid aqueous solution: the total molar addition amount of the composition material is in the range of 0.1 to 1.2 mol/L, and the amount of the masking aid aqueous solution added can be controlled to 100 parts by weight of absolute dry hydrophilic decomposable fiber A , add 1 to 2 parts by weight of the masking additive aqueous solution; or add a regular amount of ordinary anti-mold additives to the final product.

5. The co-production method of "main product A--hydrophilic decomposable fiber product" and "by-product C--lignin/resin mixture product" in the product set described in technical solution 1, the characteristics of which at least include: making A and C-1 can be co-produced by going through the following steps 5-1 or/and 5-2; or A and C-2 can be co-produced by going through the following steps 5-3 or/and 5-4 or/and 5-5. step; take last 5-6 steps to achieve:

5-1. Use fresh energy grass to remove the whole plant with roots and leaves or peel off the stem parts of the leaves, wash it with clean water, dehydrate and dry it, and then press it into a juicer. It is better to control the pressing. The moisture content of the final slag is below 20% (wt%), and the liquid squeezed out is the by-product material 2 described in item ii of technical solution 2 - "fresh energy grass washed with water first and then pressed. "The obtained fresh juice"; or this "fresh juice" can be heated to 100-105℃ for 3-5 minutes, cooled and canned to obtain a liquid black brown edible or medical grade lignin/resin mixture product C- 1; If the "fresh juice" is subjected to an evaporation and concentration operation while heating, the steamed and concentrated material of the "fresh juice" can be cooled to room temperature under the control process parameters of controlling the amount of steamed water. The edible or medical grade lignin/resin mixture product C-1 can be in the form of a paste-like tan colloid, or a coffee-colored powder or granules, or a rosin-like solid block;

5-2. Use the energy grass that has been sun-dried or naturally dried or oven-dried to remove the whole plant with roots and leaves or remove the stem part of the leaves, or use the dry energy grass material to remove 28% by crushing and screening After sieving the coarse material into fine powder, wash it with clean water. You can add water ranging from 0.7 to 5.7 times the weight of the dry material, heat it to 70°C or even boil it, and then press it into a juicer. It is better to control the amount of water after squeezing. The moisture content of the residue is below 20% (wt%), and the liquid squeezed out is the by-product material 2 described in item ii of technical solution 2 - "dry energy grass is washed with water and then boiled and pressed." "Obtained juice"; or heat the "energy grass" "juice" to 100-105℃ for 3-5 minutes, cool and can it to become a liquid black brown edible or medical grade lignin/resin mixture product C-1; If the "energy grass" and "juice" are subjected to an evaporation and concentration operation while heating, the "energy grass" and "juice" can be evaporated under the control of process parameters that control the amount of steamed water. When the concentrated material is cooled to room temperature, it can be in the form of a tan colloid in the form of pasta, or in the form of coffee-colored powder or granules, or in the form of rosin-like solid blocks, edible or medical grade lignin/resin mixture product C-1;

5-3. Use fresh energy grass wet material to remove the roots and leaves of the whole plant or remove the stem parts of the leaves, and then squeeze it into a juicer. It is better to control the moisture content of the residue after pressing to be 20 % (wt%) or less, the squeezed liquid is either the by-product material 2 described in item ii of technical solution 2 - "fresh energy grass" and "fresh juice obtained by pressing"; or the "fresh juice" "Heat to 100~105℃ and hold for 3~5 minutes, cool and can the liquid black brown feed or industrial grade lignin/resin mixture product C-2; if it is heated at the same time, then "fresh" "Juice" is subjected to an evaporation and concentration operation, and under the control of process parameters that control the amount of steamed water, the steamed and concentrated material of "fresh juice" can be in the form of a brown colloid like a pasta sauce when it is cooled to room temperature, or Feed or industrial grade lignin/resin mixture product C-2 in the form of brown powder or granules, or rosin-like solid blocks;

5-4. Use the whole plant with roots and leaves removed from the energy grass that has been sun-dried or naturally dried or oven-dried, or use the stem material with the leaves peeled off, or use the dry energy grass material only after crushing and screening. After passing through a 28-mesh sieve, the coarse material can be added with 0.7 to 5.7 times the weight of the dry material in water, heated to 70°C or even boiled, and then pressed in a juicer. It is better to control the moisture content of the residue after pressing. Below 20% (wt%), the liquid squeezed out is either the by-product material 1 described in item ii of the technical solution 2 - the brown/black liquor discharged from the hot water delignification/resin process; or the "brown liquor" /Black liquor" is heated to 100~105℃ for 3~5 minutes, cooled and canned to obtain a liquid black brown feed or industrial grade lignin/resin mixture product C-2; if it is heated at the same time, then The "brown/black liquor" is subjected to an evaporation and concentration operation, and under the control of process parameters that control the amount of steamed water, the "brown/black liquor" can be evaporated and concentrated, and then when cooled to room temperature, it can be turned into a pasta sauce The feed or industrial grade lignin/resin mixture product C-2 is in the form of brown colloid, or coffee-colored powder or granules, or rosin-like solid block;

5-5. Collect and remove the water after "washing with clean water" mentioned in item 5-1 or/and 5-2 above, use this water to wash the cow dung, remove impurities that pass through a 28-mesh sieve, and remove Obtain the crude fiber that has not passed 28 sieves after being washed with water, boil it to kill the cellulolytic enzymes in it, and then put it into a juicer for squeezing. It is better to control the output after squeezing. The moisture content of the slag is below 20% (wt%), and the liquid squeezed out is the by-product material 1 described in item ii of the technical solution 2 - the brown/black liquor discharged from the hot water delignification/resin process; or Heat the "brown/black liquor" to 100-105°C for 3-5 minutes, cool it, and can it to form a liquid black brown feed or industrial grade lignin/resin mixture product C-2; if it is heated At the same time, the "brown/black liquor" is subjected to an evaporation and concentration operation, and the "brown/black liquor" can be evaporated and concentrated under the control process parameters of controlling the amount of steamed water. When cooled to room temperature, it can be a feed or industrial-grade lignin/resin mixture product C-2 that is in the form of a paste-like brown colloid, or a coffee-colored powder or granule, or a rosin-like solid block; for cow dung The washed/washed liquid discharged after the washing/washing treatment can at least be used as direct irrigation water for planting the fertilizer-resistant and water-consuming Giant Junca grass;

5-6. The slag mentioned in the above 5-1 to 5-5 "It is better to control the moisture content of the slag after pressing to be below 20% (wt%)" can be soaked into a solid content of 25%. The loose floss-like material is sifted out and the particle size classification or mixed elongated fiber bundles ranging from 3 mesh to no more than 28 mesh can be obtained as described in step 4 of technical solution 4. "The moisture material of the hydrophilic decomposable fiber intermediate product A to be treated to remove the water solute in the fiber" can be followed by the fifth to tenth steps in the technical solution 4, and finally the hydrophilic decomposable fiber product A-1 or A-2; The water containing cow dung produced by "washing cow dung" and "washing and sieving with water" described in the aforementioned 5-5 is the "water containing cow dung" described in item ii of technical solution 2. By-product material 3: "The washing liquid produced by washing cow dung" can be directed to be one of the ingredients of the "auxiliary product E--liquid organic soil conditioner" described in the technical solution 1.

6. The preparation method of "B--wood-plastic composite recycled coarse-grained product" in the product set described in technical solution 1 is characterized by the following 6-1 to 6-6:

6-1. Material preparation: For the slag mentioned in any one of 5-1 to 5-5 in Technical Solution 5, "It is better to control the moisture content of the slag after pressing to be below 20% (wt%)", Prepare the "wood" material in "Wood Plastic Composite Regenerated Coarse Grains";

Or/and use dry energy grass that has not been pressed, and only crush or cut into sections once, then winnow or/and screen, and select materials with less nutrients to make "Wood-Plastic Composite Regenerated Coarse Grain" The "wood" is prepared, and the remaining materials with more nutrients are used as organic fertilizer or/and feed materials; the "materials with less nutrients", in terms of measurement, are the materials that have been crushed or cut into pieces after one Finally, the crude energy grass fiber that can withstand the mechanical crushing force without being more finely divided and passes through a sieve ranging from 3 to 28 mesh, and the fine energy grass that has a higher soil content in the crushed energy grass that passes through a 150 mesh sieve. Fiber powder; the "materials with more nutrients", in terms of measurement, are materials that cannot withstand the mechanical crushing force and are more finely crushed after being crushed or cut into pieces once, and pass through a sieve ranging from 28 to no more than 150 mesh. Energy grass fiber powder with small soil content and medium particle size;

Waste plastic raw materials purchased or/and collected for free, which are in a compressed and packaged state or/and which contain large pieces of metal or brick-like solids, must first be crushed and winnowed to loosen the materials. and remove hard solids such as metal and bricks; use the fluffy waste plastic with impurities removed as the "plastic" material in "wood-plastic composite recycled coarse particles";

6-2. Ingredients: According to the proportion of "wood", "plastic" and softener in the total weight of the product in the composition of "wood-plastic composite regenerated coarse particles" described in 3-4 or 3-5 in Technical Plan 3 Ratio, weigh ingredients;

6-3. Granulation: The materials prepared by the scale are passed through the mixing aggregate bin, and then transported by machinery, and put into the "coarse granulator" described in 3-7 and 3-8 of Technical Plan 3 to form Granules; the machinery used in the "coarse granulator" is: any of the feed pellet machine, organic fertilizer granulator, biomass fuel pellet machine with continuous inlet/output function, or any of the above-mentioned The "granulator"/"granulator" is then connected in series with a spiral granulator and intermediate crusher; the aforementioned "granulator"/"granulator" discharges the material in the form of segmented granules formed by the through-hole die. For example, the aforementioned "granulator"/"granulator" The "segmented granular" "materials" are then processed by the spiral granulator in series, and then the materials come out of the machine as irregular particles; the materials during granulation are heated by mechanical extrusion/friction, and can be used to feed the materials or /The water is added to the interlayer in the machine to control the outgoing material to not exceed 110°C; the "coarse wood-plastic composite recycled material" produced by this operation has a texture that can be directly pulled/pulled by human fingers/palms/ Low strength when kneaded/torn into pieces; its granulated shape at least includes segmented granules or irregular particles formed by a through-hole mold; the hole shape of the "hole mold" includes at least equilateral or unequal side lengths Any one of 3 to 12 sides, or round; the size of the "grain" is classified or mixed in any aperture ranging from 25mm to less than 2.0mm mesh;

6-4. Homogenization and mixing: If the "wood-plastic composite recycled coarse particles" obtained in item 6-3 have obvious quality defects such as inhomogeneous packaging after subsequent packaging, they can be added before weighing and packaging. Mixing and homogenizing treatment, the above-mentioned treatment is to use a mechanical roller to introduce the "wood-plastic composite recycled coarse particles" obtained in item 5-3, and tumble and mix evenly;

6-5. Weighing and packaging: The "Wood-Plastic Composite Regenerated Coarse Quality" obtained in items 6-3 or/and 6-4 that meets the quality requirements "Particles" are weighed and then introduced into packaging bags with specifications approved by market customers;

6-6. Inbound quality inspection: Put the packaged products into the warehouse in order, and provide quality inspection reports for each batch of incoming products for archiving according to the indicators that market customers need to know.

7. The preparation method of "auxiliary products" D to I in the product set described in technical solution 1, which is characterized by the following: 7-1 to 7-6:

7-1. The preparation method of "auxiliary product D - solid organic soil conditioner product" described in technical solution 1 is at least characterized in that: when using energy grass, or energy grass and cow dung as the starting main raw materials, use extracted The remaining materials after making the main product A, including energy grass powder or fine cow dung sediment that has passed through a 28-mesh sieve, are used as one of the ingredients in "auxiliary product D";

7-2. The preparation method of "auxiliary product E--liquid organic soil conditioner product" described in technical solution 1, is at least characterized by: using energy grass, or energy grass and cow dung as the starting main raw materials, during the preparation of " When the main product A - hydrophilic decomposable fiber product" and "by-product C - lignin/resin mixture product", the pressing liquid or/and washing liquid or/and elutriation liquid discharged from the upgraded products A and C ; Then the liquid organic soil conditioner product obtained by blending the "pressed liquid or/and washing liquid or/and elutriation liquid" according to the soil improvement requirements of the crops and plots being applied; the "discharge" The press liquid or/and washing liquid or/and elutriation liquid”, the pH value does not exceed the range of 5.0 to 9.4, and the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained therein are equal to those of the The liter volume ratio of water is ≤0.034mol/L, or the total wt% concentration of soluble sodium salts, potassium salts, and magnesium salts contained therein is ≤0.20% (wt%), or the soluble sodium salts, potassium salts contained therein are The difference between the total concentration of salt and magnesium salt and the total concentration of soluble sodium salt, potassium salt and magnesium salt in the water source taken from the production site is ≤0.01% (wt%); the weight ratio of auxiliary product E to main product A is Control within the range of product E/product A ≤ 100/100 ~ 300/100, that is, ≤ 100/100 or ≤ 300/100;

7-3. The preparation method of "auxiliary product F - fermented feed product" described in technical solution 1, which is at least characterized in that: the "by-product material 1: hot water delignification/resin" described in item ii of technical solution 2 The brown/black liquor discharged from the process" or/and" or by-product material 2: The fresh juice obtained by squeezing the fresh energy grass will be mixed with the energy grass that has only been broken/crushed, and then fermented to obtain auxiliary products F;

7-4. The preparation method of "auxiliary product G - pellet feed product" described in technical solution 1 is at least characterized in that: when using unpressed dry energy grass as the starting main raw material, the main raw material is screened out. The remaining materials after using the raw materials for Product A are "fine powder passed through a 28 mesh sieve", or/and "energy grass fiber powder with a small soil content and a medium particle size passed through a 28 mesh to no more than 150 mesh sieve", as particles. Ingredients in feed products;

7-5. The preparation method of "auxiliary product H--biomass pellet fuel product" described in technical solution 1 is at least characterized by: using energy grass to crush and sieve to remove fine fibers that have not passed the 28-mesh sieve. Powder, or a full-component energy grass crushing material, as an ingredient component, or a biomass pellet fuel product with waste plastics added; the "waste plastics" include at least waste agricultural plastic films and waste foam plastics , any one or more combinations of waste chemical fiber fabrics or/and chemical fiber wadding, the "addition" accounting for less than 5% of the total weight of the auxiliary product H, or up to no more than 22%;

7-6. The preparation method of "auxiliary product I - edible fungus planting stick/block product" described in technical solution 1 is at least characterized in that: when using energy grass, or energy grass and cow dung as the starting main raw materials, use The remaining materials after sifting out the raw materials for the main product A, namely energy grass powder or fine cow manure sediment that has passed through a 28-mesh sieve, are used as ingredients in the edible fungus planting stick/block product.

8. The equipment used in the "preparation method" described in technical solutions 4 to 7 is also characterized by the following 8-1 to 8-4 or 8-5:

8-1. Implementing "step one" to "step ten" described in technical solution 4 involves setting up combination machinery I to Machinery Ⅰ, which at least includes: crushing machinery 1, any one or more combinations of saw/mill/cut/hammer crusher 2, air separation machinery 3, and mechanical screen 4 to crush the energy straw bundles Machine, any one or more combinations of sawing/milling/cutting/hammer crushing machine processing, and then through air selection and screening, screen out any energy grass crushed materials that pass the 3 mesh to the 28 mesh sieve range. One-mesh classification or mixed particle size elongated fiber bundles; or an expansion machine 5 is installed after the mechanical screen 4;

The combined machine II for the "first batching" of the "step two" described in the technical solution 4, at least includes: a batching bin 6 for placing the "backup energy grass crumbs", containing the "first batching" described in the subsequent step seven. A liquid tank 7 for the extruded water obtained from "secondary solid-liquid separation", or a bin 8 for storing "surfactant", a weighing scale 9, and a mixing and stirring device after the "first batching" device 10;

The combined machine III for implementing the "heated dissolution" of "step three" described in technical solution 4, at least includes: a tank 11 for stirring, mixing, heating and insulation;

The combined machinery IV for implementing the "first solid-liquid separation" of "step four" described in technical solution 4, at least includes: a conveying machine 12, a screw or roller squeezer 13, and a solid-liquid separator 14, Storage tank 15 for storing the "pressed/extruded brown/black liquor" obtained from the "first solid-liquid separation";

The combined machine V for the "second batching" of the "step five" described in the technical solution 4, at least includes: a storage bin 16 for "tidal material to be processed of the hydrophilic decomposable fiber intermediate product A", containing The liquid tank 17 of the extruded water obtained in the "third solid-liquid separation" described in the subsequent step ten, or the silo 18 for storing the "whisker additive", the weighing scale 19, and the "third solid-liquid separation" are set up. Mixing mixer 20 after "secondary batching";

The combined machine VI for "grinding and latent elimination" in "step six" described in technical solution 4, which at least includes: setting up a high-consistency refiner 21, and setting a to-be-processed machine in front of the feed port of the high-consistency refiner 21 The material storage bin 22 is provided with a conveying mechanism or conveying machinery 23 between the storage bin 22 and the high-consistency refiner 21; after the outlet of the high-consistency refiner 21, a heat preservation or heating function is provided The submersion elimination tank 24 is provided with a conveying mechanism or conveying machinery 25 between the outlet of the high-consistency refiner 21 and the feed inlet of the submersion elimination tank 24;

The combined machinery VII for implementing the "second solid-liquid separation" of "step seven" described in technical solution 4 at least includes: a conveying machine 26, a screw or roller squeezer 27, and a solid-liquid separator 28, Storage tank 19 for storing the "extruded water obtained from the 'second solid-liquid separation'" described in step seven of technical solution 3;

The combined machine VIII for the "third batching" of "step eight" described in the technical solution 4, which at least includes: setting up and storing the moisture of the "hydrophilic decomposable fiber intermediate product B to be processed" described in the seventh step of the technical solution 4. The storage silo 29 of "material", the storage tank 30 for measuring and storing new water and circulating purified water, the silo 31 for storing whisker additives, the weighing scale 32, and the stirring and mixing tank 33;

The combined machine IX for "stirring and washing" of "step nine" described in technical solution 4, which at least includes: a conveying mechanism or conveying machine 34, screw or roller extruder is provided after the aforementioned "stirring and mixing tank 33" Pulp machine 35, material temporary storage tank 36;

The combined machinery X for implementing the "third solid-liquid separation or final modification" of "step ten" described in technical solution 4, at least includes: setting up a conveying mechanism or conveying machine 37, a solid-liquid separator 38, and setting up a storage cover The trough 39 for iron/manganese ion additives and the trough 40 for storing anti-mildew additives;

8-2. The equipment used to implement the "joint production method" described in technical solution 5 involves setting up combined machinery XI to XIII:

The combined machinery XI used to implement the "co-production of A and C-1" described in 5-1 and 5-2 of technical solution 5, at least includes: for the specific production method described in 5-1 of technical solution 5, set An operating machine 41 is used to remove roots and leaves of fresh energy grass. A cleaning machine 42 is provided for washing, dehydrating and drying the fresh energy grass. A press 43 is provided for squeezing and extracting juice from the fresh energy grass. Set up a storage tank 44 to store the fresh juice of pressed energy grass, or set up a distillation kettle 45 for heating the fresh juice to boiling or evaporation and concentration, and set up cooling and canning machinery 46;

And for the specific production method described in 5-2 of technical solution 5, an operating machine 47 for removing roots and blades of dry energy grass is provided, or a combined machine 48 for crushing and screening the dry energy grass material is provided. , set up a cleaning machine 49 for washing and dehydrating the dried energy grass, a combined machine 50 that can add water, heat it to boiling, and then extract the juice, and a storage tank 51 for storing the squeezed energy grass juice, The "energy grass juice" is also the by-product material 1 described in item ii of the technical solution 2 - the brown/black liquor discharged from the hot water delignification/resin process; or it is further configured to process the "energy grass juice" Heat to boiling or steam The concentrated distillation kettle 52 is equipped with cooling and canning machinery 53;

The combined machinery XII used to implement the "co-production of A and C-2" described in 5-3 to 5-5 of technical solution 5, which at least includes: for the specific production method described in 5-3 of technical solution 5, set An operating machine 54 for removing roots and leaves of fresh energy grass is provided, a press 55 for pressing fresh energy grass to extract juice is provided, a storage tank 56 for storing the fresh juice of the pressed energy grass is provided, or a press 55 for extracting juice from the fresh energy grass is provided. The distillation kettle 57 is heated to boiling or evaporated for concentration, and is equipped with cooling and canning machinery 58;

In view of the specific preparation method described in 5-4 of the technical solution 5, an operating machine 59 for removing roots and blades of dry energy grass is provided, or a combined machine 60 for crushing and screening the dry energy grass material is provided. Set up a combined machine 61 that can add water, heat it to boiling, and then extract the juice, and set up a storage tank 62 to store the squeezed energy grass juice; or set up a device that heats the "energy grass juice" to boiling or evaporates and thickens it. Distillation kettle 63, equipped with cooling and canning machinery 64;

In view of the specific preparation method described in 5-5 of the technical solution 5, a storage tank 65 is provided for storing the dewatered water after "cleaning" the energy grass in the combined machine XI, and a storage tank 65 is provided. A combined machine 66 for washing and screening cow dung with outflow water, a combined machine 67 for adding water, heating to boiling, and then squeezing the juice, and a storage tank 68 for storing the squeezed energy grass juice; or A distillation kettle 69 for heating the "energy grass juice" to boiling or evaporation and concentration, and a cooling and canning machine 70;

The combined machinery XIII used to implement the details of "can be walked again" and "can be guided later" described in 5-6 of the technical solution 5, at least includes: setting up a classification collection bin 71, setting up the aforementioned "output after pressing" A combined machine 72 for stirring and heating the "slag" into a loose floss-like material with a solid content of 25%; a mechanical sieve 73 is set up to collect "slender and slender particles that pass through the 3 mesh to no more than 28 mesh sieve range for particle size classification or mixing" A collection bin 74 of "shaped fiber bundle"; a conveying mechanism 75 is provided to guide the materials in the collection bin 74 to the "storage bin 16" of the aforementioned "combined machine V", and a collection tank 76 is provided;

8-3. The equipment used to implement the "Preparation Method" of "B" mentioned in Technical Solution 6 involves setting up sub-assembly machines XIV to XVII, including:

Set up the "material preparation" sub-assembly device XIV of 6-1 in the technical solution 6, which also includes: a mechanical screen 77, or a crushing machine 78 and a winnowing machine 79;

Set up the "ingredients" sub-assembly device ⅩⅤ for implementing 6-2 in the technical solution 6, which also includes: a weighing scale 80, respectively storing "wood" and "plastic" in the composition of the "wood-plastic composite recycled material coarse particles" And the storage bin 81 of the softener, and the mixing tank 82 after metering and batching;

Set up the "granulation" sub-assembly device XVI for implementing 6-3 in technical solution 6, which also includes: conveying machinery 83 and coarse granulator 84;

Set up and implement the "homogenizing and mixing" and "weighing and packaging" sub-assembly devices XVII of 6-4 to 6-5 in the technical solution 6, which also include: a homogenizing and mixing machine 85 and a weighing and packaging machine 86;

8-4. The equipment used to implement the "manufacturing method" of the "auxiliary products" described in Technical Solution 7 involves setting up sub-assembly machines XVIII to IIIII, including:

Set up the sub-assembly device XVIII used in the preparation method of 7-1 "auxiliary product D--solid organic soil conditioner" in the technical solution 7, which is characterized in that: it includes a set of assembly devices 87 for preparing solid organic soil conditioner;

Set up the sub-assembly device XIX used to implement the 7-2 "auxiliary product E--liquid organic soil conditioner" preparation method in the technical solution 7, which is characterized in that: it includes a set of assembly devices 88 for preparing liquid organic soil conditioner products;

Set up the sub-assembly device II X used in the preparation method of 7-3 "auxiliary product F--fermented feed" in the technical solution 7, which is characterized in that: it includes a set of assembly device 89 for preparing fermented feed products;

Set up the sub-assembly device II I used to implement the 7-4 "auxiliary product G-pellet feed" preparation method in the technical solution 7, which is characterized by: including a set of assembly devices 90 for preparing pellet feed products;

Set up a sub-assembly device II II used to implement the preparation method of 7-5 "auxiliary product H - biomass pellet fuel" in the technical solution 7, which is characterized by: including a set of assembly devices 91 for preparing biomass pellet fuel products;

Set up the sub-assembly device II III used to implement the 7-6 "auxiliary product H--biomass pellet fuel" preparation method in the technical solution 7, which is characterized by: including a set of assembly devices 92 for preparing edible fungus planting rods/block products;

8-5. Alternatively, each unit of machinery from 1 to 88 as described in 8-1 to 8-4 above can be arranged neatly into a standard container.

9. The uses of the “products” or/and “preparation methods” or/and “equipment” described in technical solutions 1 to 8 include at least any one or a combination of more of the following:

9-1. The "Main Product A - Hydrophilic Decomposable Fiber" described in Technical Schemes 1 and 2 can at least be used to prepare rice paper, corrugated paper, cardboard, or/and include egg trays and convenient dinner plates/bowls. It can be used as an alternative material to partially or completely replace waste paper recycled pulp in paper molded products such as paper seedling pots/bowls, etc.; it can also be used as a new starting material for further processing, such as making bleached pulp; or It is used as raw material for preparing cellulose ether;

9-2. The "by-product B - wood-plastic composite recycled coarse particles" described in technical solutions 1 and 3 can be used at least as wood plastic particles to be modified or/and refined for hot extrusion of wood-plastic products. raw material, or directly used as a new formulation raw material for hot extrusion wood plastic products, or as a granular fuel for heating;

9-3. The "by-product C-1 - edible or medical grade lignin/resin mixture" described in technical solution 1 can be used at least as a raw material for preparing beverages or/and traditional Chinese medicine preparations;

9-4. The "by-product C-2 - feed or industrial grade lignin/resin mixture" described in technical solution 1 can be used at least as a feed raw material, or/and as a water-reducing agent for concrete and rubber. /Any kind of softener in plastics;

9-5. The "products", "preparation methods" and "equipment" described in technical solutions 1 to 8 can at least be used for the "raw materials" described in item i of technical solution 2, including Giant Juncao, etc. Processing; or be expanded to the processing of bamboo, sugar cane peel, etc.;

9-6. The "products", "production methods" and "equipment" mentioned in technical solutions 1 to 8 can all become independent commodities.

10. The business operation model of the “product” or/and “process” described in any one or more of technical solutions 1 to 9, at least includes any one or a combination of the following:

10-1. One enterprise can independently implement the commercial operation of "products" or/and "manufacturing methods";

10-2. Multiple companies can divide "product" varieties, or/and segment "manufacturing" processes to collaboratively implement commercial operations;

10-3. The business model of self-operated or outsourced manufacturing can be used to implement the commercial operation of "products" or/and "manufacturing methods";

10-4. The described commercial operations, which use agricultural products including solid/liquid organic soil conditioners, and barter with farmers or farming operators for energy grass including straw from grain, cotton and oil fields.

Description of the drawings

Figure 1 is a black and white photo of the elongated fiber bundles of Mulberry branch Ya, one of the mixed energy grasses with particle sizes ranging from 3 mesh to 28 mesh.

Figure 2 is a black and white photo of the elongated fiber bundles of rice straw, one of the mixed energy grasses, which has passed through a sieve of 3 mesh to 28 mesh.

Figure 3 is a black and white photo of a dry mass sample of hydrophilic and decomposable fiber A-1, which was prepared in the laboratory from Paeonia oleifera straw, one of the energy grasses.

Figure 4 is a black and white photo of a dry mass sample of hydrophilic decomposable fiber A-2, which was prepared in the laboratory from mulberry branch Ya, one of the energy grasses.

Figure 5 is a black-and-white photo of the actual broken paper after being made from wheat straw, one of the energy grasses, into hydrophilic decomposable fiber A-2 in the laboratory. The paper was folded and unfolded after being grasped once. .

Figure 6 is a black and white photo of by-product C-2, a feed or industrial grade lignin/resin mixture that can be formulated for application Feed additives, plant nutrients, or used as rubber/plastic additives, etc.

Figure 7 is a black-and-white photo of plastic film materials discarded from waste paper to recycled pulp.

Figure 8 is a black and white photo of wood plastic composite recycled coarse grain B.

Figure 9 is a black and white photo of a dry dough standard sample.

Figure 10 is the "standard sample" described in Figure 9, which is derived from the feces of beetle larvae or wood moth larvae that eat the willow stems accumulated on the ground under a willow tree in nature. This is the "feces" under the willow tree. The black and white photo, the arrow in the photo points to the "feces".

Figure 11 is a black and white photo of what the "standard sample" described in Figures 9 and 10 looks like when it is collected in the laboratory and has not been screened or processed. Its true color is brown.

Figure 12 is a black and white photo of the scraps produced by comparing the standard sample in Figure 9 and the sample in Figure 4.

Figure 13 is a schematic block diagram of the ten steps for preparing "main product A--hydrophilic and decomposable fiber".

Figure 14 is a block schematic diagram of the process equipment flow used in the product assembly manufacturing method of the present invention, in which I to X located in the δ block surrounded by "·-" are the process equipment flow used to prepare the main product A, as shown in Ⅺ to to XVII are the process equipment flows used to prepare by-product B, and XVIII to II III in the block surrounded by "·-" are the process equipment flows used to prepare auxiliary products D to I. The definition of the numbers in the figure is:

Ⅰ is the sub-combination machinery for "pretreatment and preparation" of "Step 1" in the preparation of main product A, which at least includes: 1--crushing machinery, 2--any or more combinations of sawing/milling/cutting/hammer crushing Chemical machine, 3--Wind separation machinery, 4--Mechanical screen, 5--Puffing machinery;

Ⅱ is a sub-assembly machine for preparing the "first batching" of "step two" in main product A, which at least includes: 6--the batching bin for "backup energy grass crumbs", 7--containing the ingredients for the subsequent step seven. The liquid tank of the extruded water obtained from the "second solid-liquid separation", 8--the silo storing the "surfactant", 9--the weighing and measuring instrument, 10--the "first batching" The final mixing agitator;

Ⅲ is the sub-assembly machinery for the "heating and dissolution" of "Step 3" in the preparation of main product A, which at least includes: 11--tanks for stirring, mixing, heating and insulation;

Ⅳ is the sub-assembly machinery used for the "first solid-liquid separation" in "Step 4" in the preparation of main product A, which at least includes: 12--conveying machinery, 13--screw or roller extruder, 14-- Solid-liquid separator, 15--a storage tank that stores the "pressed/extruded brown/black liquor" obtained from the "first solid-liquid separation";

Ⅴ is the sub-assembly machine for preparing the "second batching" of "Step 5" in the main product A, which at least includes: 16--the storage bin of "the moisture material of the hydrophilic decomposable fiber intermediate product A to be processed", 17 --The liquid tank containing the extruded water obtained from the "third solid-liquid separation" described in the subsequent step ten, 18--The silo storing the "whisker additive", 19--Weighing and measuring instruments, 20 --Mixing mixer 20 after "second batching";

Ⅵ is the sub-assembly machine for "grinding and latent elimination" in "Step 6" in the preparation of main product A, which at least includes: 21--high-consistency refiner, 22--storage silo for materials to be processed, 23-- Conveying mechanism or conveying machinery 23; 24--submersible tank with insulation or heating function 25--conveying mechanism or conveying machinery;

Ⅶ is the sub-assembly machinery for the "second solid-liquid separation" in "Step 7" in the preparation of main product A, which at least includes: 26--conveying machinery, 27--screw or roller extruder, 28-- Solid-liquid separator;

Ⅷ is a sub-assembly machine for the "third batching" of "Step 8" in the preparation of main product A, which at least includes: 29--a storage silo for storing "the moisture material of the hydrophilic decomposable fiber intermediate product B to be processed", 30 is a storage tank for measuring and storing new water and circulating purified water, 31--silo for storing whisker additives, 32--weighing instrument, 33--stirring and mixing tank;

Ⅸ is a sub-assembly machine for "stirring and washing" in "Step 9" in the preparation of main product A, which at least includes: 34--conveying mechanism or conveying machinery 34, 35--screw or roller squeezer, 36-- Material temporary storage tank;

Ⅹ is the combined machinery for the "third solid-liquid separation or final modification" in "Step 10" in the preparation of the main product A, which at least includes: 37--conveying mechanism or conveying machinery, 38--solid-liquid separator, 39 --Trough for storing iron/manganese ion masking additives, 40--Trough for storing anti-mildew additives;

ⅪMachines and sub-combinations used in the co-production method of main product A and by-product C-1, including at least: 41--operating machinery for removing roots and leaves of fresh energy grass 41, 42--for fresh energy Cleaning machinery for washing, dehydrating and drying grass, 43--a press for squeezing and extracting juice from "fresh energy grass after washing with water", 44--a storage tank for storing the fresh juice of pressed energy grass, 45 --Stills for heating fresh juice to boiling or evaporating and thickening it, 46--cooling and canning machinery;

47--A machine for removing roots and leaves from dry energy grass. 47, 48--A combined machine for crushing and screening dry energy grass material. 49--A machine for washing and dehydrating dry energy grass. Cleaning machinery, 50--a combined machine that can add water, heat it to boiling, and then squeeze it out, 51--a storage tank for storing squeezed energy grass juice, 52--heat the "energy grass juice" to boiling Or distillation kettle for evaporation and concentration, 53--cooling and canning machinery;

Ⅻ Machinery used in the joint production of main product A and by-product C-2 and sub-combination machinery, including at least: 54--operating machinery for removing roots and leaves of fresh energy grass, 55--making fresh energy grass A press for squeezing and extracting juice, 56 - a storage tank for storing the fresh juice of pressed energy grass, 57 - a distillation kettle for heating the fresh juice to boiling or evaporation and concentration, 58 - cooling and canning machinery;

59--A machine for removing roots and leaves from dry energy grass, 60--A combined machine for crushing and screening dry energy grass materials, 61--It can add water, heat it to boiling, and then make juice. Combined machinery for extracting and squeezing, 62--storage tank for storing pressed energy grass juice, 63--distillation kettle for heating "energy grass juice" to boiling or evaporation and concentration, 64--cooling and canning machinery;

65--A storage tank used to store the water removed from the "clean water" of the energy grass in the combined machine XI, 66--A combined machine for washing and screening cow dung, 67--It can be reused Add water, heat to boiling, and then make a combined machine for squeezing and extracting juice, 68--a storage tank for storing the squeezed energy grass juice, 69--a still for heating the "energy grass juice" to boiling or evaporation and concentration, 70--Cooling and filling machinery;

ⅩⅢ is a sub-assembly of machinery used for "subsequent" diversion treatment in the co-production method of main product A and by-product C, which at least includes: 71--Setting up a classification collection bin, 72--Breaking the "slag after pressing" into Combined machinery for stirring and heating loose floss-like materials with a solid content of 25%; 73--mechanical screen, 74--collection bin; 75--conveying machinery, 76--collection tank;

Ⅹ Ⅳ is a sub-assembly device for "material preparation" in the production method of by-product B, which also includes: 77--mechanical screen, 78--crushing machinery, 79--wind separation machinery;

Ⅹ Ⅴ is the "ingredient" sub-assembly device in the by-product B production method, which also includes: 80--weighing instrument, 81--respectively store the "wood" and "plastic" in the composition of the "wood-plastic composite recycled material coarse particles" "And the storage silo of softener, 82--the mixing tank after metering and batching;

Ⅹ Ⅵ is the "granulation" sub-assembly device in the by-product B production method, which also includes: 83--conveying machinery, 84--coarse granulator;

Ⅹ Ⅶ is the "homogenization mixing" and "weighing packaging" sub-assembly device in the by-product B production method, which also includes: 85--homogenization mixer, 86--weighing packaging machinery;

Ⅹ Ⅷ is the sub-assembly machinery used in the preparation method of auxiliary product D, including: 87-contains a set of assembly equipment for preparing solid organic soil conditioner;

Ⅹ Ⅸ is a sub-assembly of machinery used in the preparation method of auxiliary product E, including: 88 - a set of assembly devices for preparing liquid organic soil conditioner products;

Ⅱ and Ⅹ are the sub-assembly machines used in the preparation method of auxiliary product F, including: 89-including a set of assembly devices for preparing fermented feed products;

Ⅱ Ⅰ is the sub-assembly machinery used in the preparation method of auxiliary product G, including: 90-including a set of assembly equipment for preparing pellet feed products;

Ⅱ Ⅱ is the sub-assembly machinery used in the preparation method of auxiliary product H, including: 91-including a set of assembly equipment for preparing biomass pellet fuel products;

Ⅱ and Ⅲ are sub-assembly machines used in the preparation method of auxiliary product I, including: 92-including a set of combined devices for preparing edible fungus planting sticks/block products.

Detailed ways

The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only some of the embodiments of the technical solutions of the present invention, not all of them. Example. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts should fall within the scope of protection of the present invention.

Embodiment 1. A collection of clean products using energy grass as raw material, characterized in that: using energy grass, or energy grass and cow dung as the starting main raw materials, the process and combined equipment of clean production are integrated in series and parallel through processing sub-paths, or The device array finally produces a set of cleaning products. The "product set" is specifically composed of the main product A as described below, or a combination of the main product A and any one or two of the by-products B and C; or Main product A or by-product B/C, combined with any one or more of auxiliary products D, E, F, G, H, I:

The main product A - hydrophilic decomposable fiber, characterized by: using the aforementioned "energy grass, or energy grass and cow dung", crushed by any or more combinations of sawing/milling/cutting/hammering and then sieving to obtain the "Elongated fiber bundles of any mesh size that pass through a sieve ranging from 3 mesh to no more than 28 mesh" are used as raw materials; the brown/black liquor will be discharged during the preparation process, and the "brown/black liquor" will be discharged. The ratio of the weight part W _{brown/black liquor} of "black liquor" to the weight part W _A of the absolute dry fiber containing no more than 15% water in the main product A is W _{brown/black liquor} /W _A = 90~100~300 /100 range; and the ratio of the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained in the "brown/black liquor" to the liter volume of the water contained is ≤0.034mol/L, and its pH value is within In the range of 5.0 to 9.4, each indicator does not fall within the characteristic value range of saline-alkali land; among the additives used, the total content of any one or more of caustic alkali, ammonia, ammonium salts, peroxides, and biological enzymes is 0 ; Or use water-insoluble or poorly soluble substances as whisker additives during preparation, and implement low-ash whisker grafting/coating on the fiber surface. The "whisker additive" can be used for the main product A or its intermediate product The added amount of absolute dry fiber in 100 parts by weight is ≤1~3~5~9 parts by weight, which is ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight; the main product A ——Hydrophilic and decomposable fiber products that do not float to the surface after being put into water or stirred;

By-product B - wood-plastic composite regenerated coarse particles; characterized by: at least the above-mentioned "energy grass" is crushed by any one or more combinations of sawing/milling/cutting/hammering, and then screened. The other part: "Fine materials or/and crushed materials that pass through a 28-mesh sieve, or crushed materials that are mixed with coarse and fine materials that pass through a 3-mesh sieve", and then use them with "waste plastics" as raw materials, or mix them with those in A The above-mentioned "brown/black liquor" has a mass transfer connection and is pelletized using a biomass fuel pellet machine;

Auxiliary product D - solid organic soil conditioner, characterized by: the remaining material after extracting "energy grass, or energy grass and cow dung" that does not pass the 28-mesh sieve to make the main product A. Energy grass powder or fine cow dung sediment is used as one of the ingredients in the solid organic soil conditioner;

Auxiliary product E - liquid organic soil conditioner, characterized by: utilizing the brown/black liquor discharged during the preparation of the hydrophilic decomposable fiber main product A, or/and utilizing the discharged liquid due to the upgrading of the main product A and by-product C Pressed liquid or/and washing liquid or/and elutriated liquid, products blended according to the soil quality requirements of the crops and fields to be applied; the "discharged pressed liquid or/and and washing liquid or/and elutriation liquid" or "brown/black liquor", its pH value is in the range of 5.0 to 9.4, and the gram mole of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained therein is the same as that contained in it. The liter volume ratio of water is ≤0.034mol/L, or the total wt% concentration of soluble sodium salts, potassium salts, and magnesium salts contained therein is ≤0.20% (wt%), or the soluble sodium salts, potassium salts contained therein are The difference between the total concentration of salt and magnesium salt and the total concentration of soluble sodium salt, potassium salt and magnesium salt in the water source taken from the production site is ≤0.01% (wt%); the weight ratio of auxiliary product E to main product A is Control within the range of W _E /W _A ≤500/100 or ≤ or 2000/100 ≤ or 3000/100;

Embodiment 2. The "main product A--hydrophilic and decomposable fiber" described in Embodiment 1, its characteristics include at least the following ⅰ to ⅵ, or a combination with ⅶ:

ⅰ. Raw materials used: including Echinacea, Liba, lemongrass, Arundodis, reeds, reeds, zebra grass, elephant grass, king grass, king bamboo grass, giant fungus grass, five-jointed miscanthus, rice grass, purple elephant grass , dwarf elephant grass, red elephant grass, sweet elephant grass, grass shoots, grass sugarcane, pseudosorghum, sweet sorghum, Peter grass, Sudan grass, Taiwan sweet grass, Pennisetum alterniflora, Spartina alterniflora hybrid, American wolftail Energy grasses of any one or more combinations of grasses and hybrid pennisetum, grain, cotton, and oil crops that produce a large amount of straw - rice, wheat, corn, cotton, rape, soybean, oil peony, oil peony, sunflower, grizzly Energy grass composed of any one or more combinations of hemp straws, or any one or more combinations of willows, bamboo willows, poplars, mulberry trees, and wolfberry trees that are artificially dwarfed and whose upper branches need to be pruned all year round; After being crushed by any one or more combinations of sawing/milling/cutting/hammering and then sieving, a part of it is obtained: an elongated shape with any mesh size ranging from 3 mesh to no more than 28 mesh sieve or mixed particle size. fiber bundle fragments;

Or and by-product material 4: use activated carbon and acidic clay to adsorb and decolorize impurities in the aforementioned "brown/black liquor", and purify circulating water to obtain the decolorized adsorption sludge; or use the aforementioned "brown/black liquor", The decolorized adsorption sludge is obtained by adding sulfuric acid dropwise to acidify until the pH value does not exceed 7.0, and using activated carbon or activated carbon and acid clay to purify circulating water;

Or and by-product material 5: Use chemical or biochemical methods to precipitate the aforementioned "brown/black liquor" or/and "washing liquor" Decolorized precipitated sludge obtained from purification treatment;

ⅵ. Production process characteristics: During the production process, the ratio of the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained in the water involved to the liter volume of "water" is ≤0.034 mol/L; and adopt Impregnate the fiber material with water of not less than 70°C at least twice to remove the lignin/resin in the fiber; the flow direction of the gradually thickening brown/black liquor in the "water" flow is consistent with the flow direction of the fiber material in the production process The flow direction is countercurrent; or water-insoluble or poorly soluble substances are added as whisker additives, and the amount added accounts for 100 parts by weight of the absolute dry fiber in the main product A or its intermediate product, and is ≤1~3~5~9 parts by weight parts by weight, either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight, implement low-ash whisker grafting/coating on the fiber surface; among the additives used, caustic alkali, ammonia The total content of any one or more of ammonium salts, peroxides, and biological enzymes is 0;

ⅶ. Preferable parameters: or "The ratio of the discharged weight part W _{brown/black liquor} and the total obtained weight part W _A of the absolutely dry main product A with a water content not exceeding 15% as described in item ⅱ is W _{brown/black Liquid} /W _A = 100~120~150/100 range; or "adding water-insoluble or poorly soluble substances as whisker additives as described in item ⅵ, the amount added is equivalent to the absolute dry fiber in the main product A or its intermediate product "100 parts by weight""is ≤1~3~5 parts by weight", "either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight"; the "whisker additive" is at least a saturated aqueous solution of calcium hydroxide , any of silica sol, etc., or/and newly generated calcium hydroxide, aluminum hydroxide, hydrated silicic acid, calcium silicate, magnesium silicate, aluminum silicate, calcium carbonate, and calcium sulfate dihydrate in the aqueous phase , ferric hydroxide, etc., or/and any kaolin, clay, fly ash, wollastonite, etc. that have been ultrafinely pulverized to the point that it cannot naturally precipitate to clear surface water within half an hour in water. One or more combinations, or any one or more combinations of kaolin, clay, fly ash, wollastonite, etc. crushed to 320 mesh.

Embodiment 3. The "by-product B--wood-plastic composite regenerated coarse particles" described in Embodiment 1 is more characterized by: the characteristics of "wood" are as follows: Example 3-1 or Example 3-1 and Example 3- 2, in which the characteristic of "plastic" is the following Example 3-3 or the combination of Example 3-3 and Example 3-4, and the product dosage form characteristics are the following Examples 3-5 to 3-8:

Example 3-1. The “wood” includes a part derived from energy grass: fine materials or/and crushed materials that pass through a 28-mesh sieve, or crushed materials mixed with coarse and fine materials that pass through a 3-mesh sieve;

Example 3-2. The "part" as described in 3-1 above is the dry basis weight of the "wood" containing 15% of equilibrium water after natural drying in the air, accounting for 5% of the total weight of by-product B. to 78% (wt%);

Example 3-3. The raw materials for “plastic” are all selected from waste plastics;

Example 3-4. The "waste plastics" as described in Example 3-3 above include at least any one or more combinations as described below: Miscellaneous waste plastic film residue discarded from waste paper recycling, including the "miscellaneous waste""Plastic film residue" obtained by water flotation and floating plastic-containing materials or/and submerged plastic-containing materials; commercial plastic film waste packaging bags, cutting/punching edge materials, and waste composite plastic film materials in the production of plastic film packaging bags , trademark labeling student Plastic film composite release paper/film, waste aluminum-plastic composite film, and waste agricultural plastic film discarded during production/use; impurity-containing polymer fibers separated from broken tires, waste chemical fiber flannel removed from cars , waste chemical fiber carpets, waste chemical fiber fabrics, waste chemical fiber meltblown cloth, waste chemical fiber filter paper; waste wire plastic skins, waste plastic packaging tapes, waste plastic woven bags, waste geotextiles, waste/old plastic shoes, waste plastic flooring products , waste plastic toys, waste plastic barrels, waste plastic bottles, waste plastic geotextiles, waste/old plastic lawns, waste plastic building materials, waste plastic pipes, waste plastic boards, waste plastic stationery, waste plastic boxes/bags, waste plastic miscellaneous pieces; waste PVC artificial leather, waste PU artificial leather; waste foam plastic;

Example 3-5. The dosage form of by-product B can be set to at least the first group of A, B, C, and D, or/and the second group of E, Ji, Geng, and Xin, or/and the third group of Ren and Gui. Group, you can choose any one or more of A to Gui in the first to third groups and mix them in any ratio to make the wood-plastic composite regenerated coarse-grained downstream plastic particles easily. Or the total weight of "wood" or "wood" with "impurities" in the product is in the range of 5% to 78%; the weight ratio of the two in the aforementioned "wood with 'impurities'" is W _Impurities /W _wood =0~10/100, the “wood” is absolutely dry material with a moisture content of no more than 15%, and the “impurities” are “by-product materials” as described in ⅱ of Example 2 4" or/and "by-product material 5"; the total weight input ratio of "plastic" and softener is in the range of 22% to 95%, and the weight ratio of the two in the aforementioned "'plastic' and softener" is W _Waste _plastic /W _softener =100/0～100:

First group:

Second Group:

The third group:

Example 3-6. Or as described in Example 3-5, "Add any one or more of A to Gui in the first to third groups to control the coarse particles in wood-plastic composite regenerated matter. The total weight input of “wood” in the downstream plastic particles or products is in the range of 5% to 78%, and the total weight input of “plastic” and softener is in the range of 22% to 95%, Example 3-5 The proportion of the total weight of "wood" in each of the feeding combinations of A to Gui in the "first group", "second group" and "third group" is proportional to the total weight of "plastic" and softener. The proportion can be determined according to the customization of market customers;

Example 3-7. The "Wood-Plastic Composite Regenerated Coarse Grain" is composed of materials according to the "First Group" or/and "Second Group" or/and "Third Group" mentioned in Example 3-5. "A to Gui components in the combined ingredients are fed, and after being processed by a coarse granulator, the texture is low-strength coarse granules that can be directly pulled/pulled/pinched/teared/grabbed by human fingers/palms, as described "Low strength" refers to at least the standard sample specimen of plastic with tensile strength ≤3PMa;

Example 3-8. As mentioned in the above example 3-7, the "coarse granulator" specifically refers to any feed pellet machine, organic fertilizer granulator, or biomass fuel pellet machine with continuous feeding/discharging function. One, or a spiral granulator and intermediate crusher can be connected in series after the aforementioned "granulator"/"granulator".

Example 4. For the preparation method of "main product A--hydrophilic decomposable fiber product" in the product set described in Example 1, please refer to Figure 13--10 steps for preparing "main product A--hydrophilic decomposable fiber". A block diagram of steps, which may include Follow steps one to ten below:

Or the shredded slender fiber bundles of energy grass that have been removed and purified are subjected to mechanical expansion processing;

Step 2 - First batching: Take 100 parts by weight of the natural dry material of the "Standby Energy Grass Crushed Material" obtained in Step 1, and mix in the "Second Solid-Liquid Separation" described in the subsequent Step 7. The extruded water, the "stirring in" and "extruded water", after measuring the free content carried by 100 parts by weight of the natural bone-dry material in the solid phase obtained by the "first solid-liquid separation" described in the subsequent step 4 If the amount of water is Active agent: any one or combination of sodium butylnaphthalene sulfonate, sodium dodecylbenzene sulfonate, sodium lauryl sulfate, or/and coconut oil fatty acid diethanolamide, fatty alcohol polyoxyethylene Any one or a combination of multiple ethers; the "2x" corresponds to 100 parts by weight of the natural dry material of the energy grass saw crushed material: in the range of 25 to 50 to 300 parts by weight;

Step 4 - The first solid-liquid separation: Introduce the material after the above "heating and heat preservation operations" into a screw or roller extruder, perform a mechanical kneading treatment on the fiber bundles of the material, and then knead it. The materials are introduced into a solid-liquid separator for solid/liquid separation; or the materials after the above-mentioned heating and heat preservation operations are directly introduced into a solid-liquid separator for solid/liquid separation; thereby obtaining the "pressed/extruded brown" as described in Example 1. / black liquor", and the moisture material of the hydrophilic decomposed fiber intermediate product A to be treated, which has initially removed the water solute in the fiber;

Step 5 - Second batching: It is determined that the free water carried by 100 parts by weight of the natural dry material in the solid phase of the "moist material for the hydrophilic decomposable fiber intermediate product A" described in step 4 is x parts by weight. Then, take 100 parts by weight of the natural dry material contained in the "moist material of the hydrophilic decomposable fiber intermediate product A to be treated" and x parts by weight of free water, and then mix in the "third solidification step" described in the subsequent step ten. The extruded water obtained by "liquid separation" is not less than: Add a whisker auxiliary. The "whisker auxiliary" is at least any one of saturated aqueous calcium hydroxide solution, silica sol, etc., or/and newly generated calcium hydroxide, aluminum hydroxide, and hydrated silicon in the aqueous phase. Any one or combination of acids, calcium silicate, magnesium silicate, aluminum silicate, calcium carbonate, calcium sulfate dihydrate, ferric hydroxide, etc., or/and ultrafinely crushed to the point where it cannot be dissolved in water within half an hour. Any one or combination of kaolin, clay, fly ash, wollastonite, etc. that have naturally precipitated to a clear surface layer, or kaolin, clay, fly ash, and silica fume that have been crushed to 320 mesh Any one or a combination of stones, etc.; the "whisker additive", the amount added to 100 parts by weight of absolute dry fiber in the "moist material of hydrophilic decomposable fiber intermediate product A" is ≤ 1 to 3 ~5~9 parts by weight, that is, the added amount is ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight; mix the second ingredients described in step 5 in the mixing tank first, The materials are ready to be processed by high-concentration grinding;

Step 10 - The third solid-liquid separation or final modification: Introduce the "material to be finally squeezed dry" in the above-mentioned step 9 into the solid-liquid separator for solid/liquid separation; thus obtain the material as in the previous "step five" The above-mentioned "extrusion water obtained from the 'third solid-liquid separation'", and the final product - the hydrophilic and decomposable fiber A product including A-1 or/and A-2; or and then adding masking to the final product Iron/manganese ion additives: oxalic acid, sodium oxalate, potassium oxalate, ammonium oxalate, ethylenediaminetetraacetic acid, sodium ethylenediaminetetraacetate, tetraacetylethylenediamine, citric acid, sodium citrate, tartaric acid, sodium tartrate, A combination of any one or more of gluconic acid, diethylenetriaminepentaacetic acid, diethylenetriaminepentamethylenephosphonic acid, pentasodium diethylenetriaminepentacetate, and sodium nitrilotriacetate, so The above composition material can be formulated into a masking aid aqueous solution: the total molar addition amount of the composition material is in the range of 0.1 to 1.2 mol/L, and the amount of the masking aid aqueous solution added can be controlled to 100 parts by weight of absolute dry hydrophilic decomposable fiber A , add 1 to 2 parts by weight of masking additive aqueous solution; or add a regular amount of ordinary anti-mold additives to the final product. For specific dosage and variety, please refer to the product instructions of each merchant in the market.

As mentioned above in connection with Figure 13, the flow direction of the aqueous solution shown by the dotted line in Figure 13 is from the bottom of Figure 13 to upwards, and the direction of the fiber is from the top of Figure 13 to downwards. The brown color in the water flow /The flow direction of black liquor and the direction of fiber are On the contrary, if the amount of water added as mentioned above and the dehydration amount of three solid-liquid separations are controlled well, the hydrophilic and decomposable fiber A product can be pressed/extruded in the hot water delignification/resin process. The ratio of the final obtained weight part W _{brown/black liquor} to the total obtained weight part W _A of the absolutely dry fiber product A with a moisture content not exceeding 15% is W _{brown/black liquor} /W _A = 90 to 100 ~300/100 range.

What should be pointed out here is: if a small sample is made in the laboratory, even if solid-liquid separation is carried out by squeezing by hand, W _{brown/black liquor} /W _A = 300/100 can be achieved, but it is even more difficult to use machinery. Worry about achieving the range index of W _{brown/black liquor} /W _A = 90~100~300/100; the mixture of fiber and water is heated at least twice during the whole process, which is just like the traditional Chinese medicine taken by patients in daily life. After decoction in water for two times, it is the same reason that the ingredients of the colored liquid cannot be obtained by decoction for the third time. You can worry about the hydrophilic decomposable fiber of the present invention being used for high-consistency refining during the papermaking operation of downstream users. The water will be colored due to the high temperature generated by the friction.

What can also be pointed out here is that as mentioned in the above production method: "The material after the above heating and heat preservation operations is introduced into a screw or roller extruder, and the fiber bundles of the material are mechanically kneaded by crushing and extrusion", and "High-concentration grinding treatment"; and this "mechanical kneading treatment of crushing and squeezing the fiber bundles of the material" and "high-concentration grinding treatment", its fiber-breaking function is much weaker than the mere grinding of food. A household food grinder with a cross rotary knife, and its softening and dispersing functions of fiber are far better than that of a household grinder. After understanding this analogy relationship, the practical value of the hydrophilic decomposable fiber A of the present invention can be seen from Figures 1 to 5:

Figure 1 is a black and white photo of the elongated fiber bundles of mulberry branch Ya, one of the mixed energy grasses with a particle size ranging from 3 mesh to no more than 28 mesh. It is made of mulberry branch Ya branches discarded from the sericulture industry and is sawed/ground/cut. / Mechanical crushing treatment of any or more combinations of hammers, and obtained after sieving, this "reduced elongated fiber bundles of mulberry branches and twigs with a particle size that has passed through a sieve of 3 mesh to less than 28 mesh" , generally accounting for at least 35% of the total "broken mulberry branches";

Figure 2 is a black and white photo of the elongated fiber bundles of rice straw, one of the mixed energy grasses with particle sizes ranging from 3 mesh to no more than 28 mesh. The rice straw is shredded by a machine and screened. The obtained "slender fiber bundle fragments of rice straw mixed with a particle size of not more than 3 mesh to no more than 28 mesh sieve" can generally account for more than 30% of the total "rice straw fragments";

Figure 3 is a black and white photo of a dry mass sample of hydrophilic decomposable fiber A-1, which is produced in the laboratory from peony straw, one of the energy grasses: follow the process of Figure 13, and finally squeeze and dehydrate by hand. , the wet material still containing 75% moisture is obtained after natural drying at room temperature. It can be seen from the photo: Although the fibers in the dry dough are thick and straight, the fibers are not as soft and bendy as traditional pulp fibers and often have bifurcations, but the thick and straight fibers are firmly in contact with each other. This can be seen from the material. The aggregated group shape is not a form that can support the stable aggregation of such thick straight fibers and has a hard feeling when pinched by hand, and it is not in the shape of crumbs. It can be inferred that if the present invention uses a small amount of whisker additives, the whiskers It realizes the surface grafting/coating of the fiber, roughens the surface of the fiber, and then achieves the purpose of making the fiber in the water like Velcro to make the fiber collide or wind up smoothly to form a ball/paper. For the sample shown in Figure 3, in Step 8 of Example 4, the whisker additive used in "stirring in new water or regenerated water with decolorized impurities" is calcium hydroxide, that is, "Stir in new water or regenerated water with decolorized impurities" and "x parts by weight" to prepare a saturated aqueous solution of calcium hydroxide, and then perform the batching operation as in step 8 in Example 4. According to the added saturated aqueous solution of calcium hydroxide and the water temperature is 0°C, the maximum dissolution constant of calcium hydroxide in 100g of water is 0.185g. When CO ₂ is absorbed in the air, it will eventually be converted into calcium carbonate crystals deposited/coated on the surface of the fiber. Must; the dissolved amount of calcium hydroxide in 300g of water carried by 100g of absolutely dry fiber in the dry dough sample in Figure 3 is ≤300g _(water) × 0.185g/100g _(water) , which is converted into Weight of calcium carbonate: W _{calcium carbonate whiskers} ≤ [3×[0.185g/(40+2×17) _{calcium hydroxide molecular weight} ]×(40+12+3×16) _{calcium carbonate molecular weight} =3×[0.185 g/74 _{molecular weight of calcium hydroxide} ] × 100 _{molecular weight of calcium carbonate} = ] 0.75g; that is, the amount of whisker material in the sample in Figure 3 added to 100 parts by weight of the absolute dry fiber in the main product A is ≤ 1 part by weight . By the way, the sample in Figure 3 does not float when it enters the water.

Figure 4 is a black and white photo of a dry mass sample of hydrophilic decomposable fiber A-2, which is produced in the laboratory from Mulberry branch Ya, one of the energy grasses: follow the process of Figure 13, and finally squeeze and dehydrate by hand. First obtain the wet material that still contains 75% moisture, then press it tightly with your fingers to shape it in a disposable plastic cup, pour it out, and dry it naturally at room temperature. In the sample shown in Figure 4, the crystal The additive is wollastonite that has passed through a 320-mesh sieve. Add water to form a suspension with a solid content of no more than 20%. Then add a nearly equivalent amount of sulfuric acid or sulfonated waste sulfuric acid to react with it to generate hydrated silicic acid and sulfonated waste sulfuric acid. The composition of calcium sulfate dihydrate and a small amount of unreacted wollastonite powder is precipitated. When the pH value changes to the range of 5 to 8, the reaction is terminated. Then the already watery cement-like reaction product is added with water to form a weight of 100 A dilute suspension with a solid content of no more than 1.65 parts in water, and then add this "thin suspension" as "x parts by weight" to the ingredients in Step 8 in Example 4, so that the crystals in the sample in Figure 4 The solid material is required. For 100 parts by weight of absolute dry fiber in the final main product, the maximum amount is 3×1.65 parts by weight, which is ≤5 parts by weight. Figure 4 is a sample that does not float when it enters water.

Figure 5 is a paper sheet made from wheat straw, one of the energy grasses, which was made into hydrophilic and decomposable fiber A-2 in the laboratory. After natural drying, the paper sheet was folded and unfolded after being grasped only once. Black and white photo of the actual broken specimen. Please note: In the "broken sample" shown in Figure 5, although the hydrophilic and decomposable fibers will be broken, they will not fall apart, which shows that the technical solution of the present invention for coating whiskers is effective; "Broken solid sample", the sample preparation tool used to grind and disperse the "hydrophilic and decomposable fiber A-2" of wheat straw is a household food grinder, so the "hydrophilic and decomposable fiber A-2" of wheat straw is used While the fibers in the sample are being softened and dispersed, they are also cut in large quantities. This causes the "broken sample" to be broken due to its short fiber length during the sample preparation process of "grabbing it once by hand". Folding resistance - there are many cracks; but conservatively speaking, even in terms of the quality of such intentionally inferior preparation, use this "hydrophilic decomposable fiber A-2" sample material to partially or completely replace Waste paper recycled pulp, as a new raw material for the paper industry, also has application markets, such as corrugated paper, rice seedling raising or sowing paper, cardboard, paper molded products, etc. In the sample shown in Figure 5, the whisker additive is made of the "calcium hydroxide" and "clay" described in item vii of Example 2, plus water to prepare a dilute solution with a solid content of no more than 3 parts in 100 parts by weight of water. suspension, and then add this "thin suspension" to the ingredients in step eight in Example 4, so that the whisker solid material in the sample in Figure 5 is 100% of the absolute dry fiber in the final main product. The maximum added amount is 3×3 parts by weight, which is ≤9 parts by weight.

Furthermore, even if calcium hydroxide is used in the whisker additive provided by this technical solution, due to its small amount, it can be carbonized to generate calcium carbonate only by exposure to the air, without the need to deliberately introduce CO ₂ .

Embodiment 5. The co-production method of "main product A - hydrophilic decomposable fiber product" and "by-product C - lignin/resin mixture product" in the product set described in Example 1, the characteristics of which at least include: To co-produce A and C-1, you can first go through the steps of Example 5-1 or/and Example 5-2; or to co-produce A and C-2, you can go through the following Example 5-3 or/and Example 5-4 first. Or/and Example 5-5 steps; in the end, all are achieved by taking steps 5-6:

Example 5-1. Use fresh energy grass to remove the whole plant with roots and leaves or peel off the stem parts of the leaves, wash it with clean water, dehydrate and dry it, and then squeeze it into a juicer. It is better to control The moisture content of the residue after pressing is below 20% (wt%), and the liquid squeezed out is the by-product material 2 described in item ii in Example 2 - "fresh energy grass washed with water first and then pressed "The obtained fresh juice"; or this "fresh juice" can be heated to 100-105°C for 3-5 minutes, cooled, and canned to obtain a liquid black brown edible or medical grade lignin/resin mixture product C -1; If the "fresh juice" is subjected to an evaporation and concentration operation while heating, then under the control process parameters of controlling the amount of steamed water, the steamed and concentrated material of the "fresh juice" can be cooled to At room temperature, edible or medical grade lignin/resin mixture product C-1 can be in the form of a paste-like tan colloid, or a coffee-colored powder or granules, or a rosin-like solid block;

Example 5-2. Use the whole plant with roots and leaves or remove the stem part of the leaves from the sun-dried or naturally dried energy grass, or use the energy grass dry material to remove it through crushing and sieving. After sieving the coarse material into fine powder with a 28-mesh mesh, wash it with clean water. You can add water ranging from 0.7 to 5.7 times the weight of the dry material, heat it to 70°C or even boil it, and then press it into a juicer. It is better to control the pressing. The moisture content of the final slag is below 20% (wt%), and the liquid squeezed out is the by-product material 2 described in item ii in Example 2 - "dry energy grass is washed with water and then boiled and pressed. "Obtained juice"; or this "juice" can be heated to 100-105°C for 3-5 minutes, cooled, and canned to obtain a liquid black brown edible or medical grade lignin/resin mixture product C-1 ; If the "juice" is subjected to an evaporation and concentration operation while heating, then under the control of process parameters that control the amount of steamed water, the "juice" can be evaporated and concentrated, and then when cooled to room temperature, it can be presented as noodles. Edible or medical grade lignin/resin mixture product C-1 in the form of paste-like brown colloid, or coffee-colored powder or granules, or rosin-like solid block;

Example 5-3. Use fresh energy grass wet material, the whole plant with roots and leaves removed or the stem part with the leaves removed, and then put it into a juicer for squeezing. It is better to control the moisture content of the slag after squeezing. 20% (wt%) or less, the liquid squeezed out is either the by-product material 2 described in item ii of Example 2 - "fresh energy grass" and "fresh juice obtained by pressing"; or the "fresh juice obtained by pressing"; "Juice" is heated to 100~105℃ for 3~5 minutes, cooled and canned to obtain a liquid black brown feed or industrial grade lignin/resin mixture product C-2; if it is heated at the same time, then " "Fresh juice" is subjected to an evaporation and concentration operation, and under the control of process parameters that control the amount of steamed water, the steamed and concentrated material of "fresh juice" can be turned into a brown paste-like colloid when cooled to room temperature. Or feed or industrial grade lignin/resin mixture product C-2 in the form of brown powder or granules, or rosin-like solid blocks;

Example 5-4. Use the whole plant with roots and leaves removed from the energy grass that has been sun-dried or naturally dried or oven-dried, or use the stem material with the leaves removed, or use the dry energy grass material that has only been crushed and screened. After removing the coarse material from the 28-mesh sieve, you can add 0.7 to 5.7 times the weight of the dry material with clean water, heat it to 70°C or even boil it, and then press it into a juicer. It is better to control the content of the residue after pressing. The water content is below 20% (wt%), and the liquid squeezed out is the by-product material 1 described in item ii in Example 2 - the brown/black liquor discharged from the hot water delignification/resin process; or the " "Brown/Black Liquor" is heated to 100-105°C for 3-5 minutes, cooled, and canned to obtain a liquid black brown feed or industrial-grade lignin/resin mixture product C-2; if heated at the same time, Then the "brown/black liquor" is subjected to an evaporation and concentration operation, and under the control of process parameters that control the amount of steamed water, the "brown/black liquor" can be evaporated and concentrated, and then when cooled to room temperature, it can be presented as noodles. Feed or industrial grade lignin/resin mixture product C-2 in the form of paste-like brown colloid, or coffee-colored powder or granules, or rosin-like solid block;

Example 5-5. Collect the water removed after "washing with clean water" as described in the above Example 5-1 or/and Example 5-2, use this water to wash the cow dung, and remove the 28-mesh sieve Impurities, pick up the crude fiber that has not passed 28 sieves after being washed with water, boil it to kill the cellulolytic enzymes in it, and then put it into a juicer for squeezing. It is better to control the squeezing. The moisture content of the final residue is below 20% (wt%), and the liquid squeezed out is the by-product material 1 described in item ii in Example 2 - the brown/black liquor discharged from the hot water delignification/resin process. ; Or heat the "brown/black liquor" to 100-105°C for 3-5 minutes, cool it, and can it to form a liquid black brown feed or industrial-grade lignin/resin mixture product C-2; if While heating, the "brown/black liquor" is subjected to an evaporation and concentration operation. Under the control process parameters of controlling the amount of steamed water, the "brown/black liquor" can be evaporated and concentrated and then cooled to room temperature. Feed or industrial grade lignin/resin mixture product C-2, which can be in the form of a paste-like tan colloid, or a coffee-colored powder or granules, or a rosin-like solid block; washed/washed cow dung The washed/washing liquid discharged after treatment, which is the "by-product material 3" described in item ii of Example 2, can be used as direct irrigation water for fertilizer-resistant and water-consuming giant fungus grass, etc.;

Example 5-6. The slag described in the aforementioned Examples 5-1 to 5-5 "It is better to control the moisture content of the slag after pressing to be below 20% (wt%)" can be soaked into water containing Consolidate 25% of the loose floss-like material, sieve out the particle size classification or mixed elongated fiber bundles ranging from 3 mesh to 28 mesh, and obtain the fiber bundle described in step 4 of Example 4. "The moisture material to be treated as the hydrophilic decomposable fiber intermediate product A after initially removing the water solute in the fiber" can be followed by the fifth to tenth steps in Example 4, and finally the hydrophilic decomposable fiber product A can be obtained -1 or A-2; the water containing cow dung produced by "washing cow dung" and "washing and sifting with water" described in the aforementioned 5-5 is the same as item ii in Example 2. The above-mentioned "by-product material 3: washing/washing liquid produced by washing/washing cow dung" can be directed to be one of the ingredients of the "auxiliary product E--liquid organic soil conditioner" described in Example 1.

Figure 6 is a black and white photo of by-product C-2 - feed or industrial grade lignin/resin mixture, which can be formulated as feed additives, plant nutrients, or used as rubber/plastic additives, etc. It is used The brown/black liquor discharged from the hot water delignification/resin process in the production of hydrophilic decomposable fiber A is directly evaporated in a beaker on an electric stove in the laboratory, dehydrated and concentrated to dryness.

Embodiment 6. The preparation method of "B--wood-plastic composite recycled coarse-grained product" in the product set described in Embodiment 1 is characterized by the following Examples 6-1 to 6-6:

Example 6-1. Material preparation: For any one of Example 5-1 to Example 5-5 in Example 5, "It is better to control the moisture content of the residue after pressing to be below 20% (wt%)" The slag is used as the "wood" material in "wood-plastic composite recycled material coarse particles";

Example 6-2. Ingredients: According to the composition of the "wood-plastic composite recycled coarse particles" described in Example 3-4 or Example 3-5 in Example 3, "wood", "plastic" and softener are included in the total weight of the product. The proportion of feeding materials and weighing the ingredients;

Example 6-3. Granulation: The materials prepared by the scale are passed through the mixing and collecting bin, then transported by machinery, and put into the "coarse granulator" described in Examples 3-7 and 3-8 in Example 3. "Medium granulation; the machinery used in the "coarse granulator" is: any one of a feed pellet machine, an organic fertilizer granulator, a biomass fuel pellet machine with continuous feeding/discharging functions, or After the aforementioned "granulator"/"granulator", a spiral granulator and a secondary crusher are connected in series; the aforementioned "granulator"/"granulator" discharges the material in the form of segmented granules formed by the through-hole mold. If the aforementioned "segmented granular" "materials" are processed by a series-connected spiral granulator and secondary crusher, the materials will appear as irregular particles when they are discharged from the machine; the materials during granulation are heated by mechanical extrusion/friction and can be used Add water to the material or/and the interlayer in the machine to control the outgoing material to not exceed 110°C; the "coarse wood-plastic composite recycled material" produced by this operation has a texture that can be directly pulled by human fingers/palms / pull / pinch / tear into pieces of low strength; its granulated shape at least includes segmented granules or irregular particles formed by the through-hole mold; the hole shape of the "hole mold" includes at least equilateral or irregular Any of 3 to 12 sides with equal sides, or a circle; the size of the "grain" is classified or mixed in any aperture ranging from 25mm to less than 2.0mm mesh;

Example 6-4. Homogenization and mixing: If the "wood-plastic composite recycled coarse particles" obtained in Example 6-3 have obvious quality defects such as inhomogeneous packaging after subsequent packaging, they can be weighed before packaging. Add a mixing and homogenizing process. The process is to use a mechanical roller to introduce the "wood-plastic composite recycled coarse particles" obtained in Example 5-3, and tumble and mix evenly;

Example 6-5. Weighing and packaging: The "Wood Plastic Composite Regenerated Coarse Granules" obtained in Example 6-3 or/and Example 6-4 that meet the quality requirements are weighed and then introduced into packaging bags with specifications approved by market customers. middle;

Example 6-6. Inbound quality inspection: Put the packaged products into the warehouse in order, and provide quality inspection reports for each batch of incoming products for archiving according to the indicators that market customers need to know.

Please refer to attached Figures 7 and 8: Figure 7 is a black-and-white photo of plastic film materials discarded from recycled pulp made from waste paper. It contains impurities such as aluminum-plastic composite molds. This is the most difficult to be greened among mixed waste plastics. It is a type of continuous reuse that our country has banned the import of foreign waste paper because of the problem of waste plastic recycling pollution. Figure 8 is a black and white photo of wood-plastic composite recycled coarse grain B, which is made of the "miscellaneous" material shown in Figure 7. "Waste plastic film material" is mixed with energy grass crumbs passed through a 28-mesh sieve, or with "C-2" described in Example 5-3 to Example 5-5 in Example 5, and then the current common biomass granule production process is used. Produced by granulator.

Embodiment 7. The preparation method of "auxiliary products" D to I in the product set described in Embodiment 1, which is characterized by the following:

Example 7-1. The preparation method of "auxiliary product D - solid organic soil conditioner product" described in Example 1 is at least characterized by: using energy grass, or energy grass and cow dung as the starting main raw materials, using extraction The remaining materials after preparing the raw materials for main product A, namely energy grass powder or fine cow dung sediment that has passed through a 28-mesh sieve, are used as one of the ingredients in "auxiliary product D";

Example 7-2. The preparation method of "auxiliary product E--liquid organic soil conditioner product" described in Example 1, is at least characterized in that: energy grass, or energy grass and cow dung are used as the starting main raw materials. When "main product A - hydrophilic decomposable fiber product" and "by-product C - lignin/resin mixture product", the pressing liquid or/and washing liquid or/and elutriation discharged from the upgraded products A and C liquid; and then the liquid organic soil conditioner product obtained by blending the "pressed liquid or/and washing liquid or/and elutriation liquid" according to the soil improvement requirements of the crops and plots to be applied; the " The pH value of the discharged pressing liquid or/and washing liquid or/and elutriation liquid does not exceed the range of 5.0 to 9.4, and the gram mole of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained therein is equal to that of the The ratio of water to liter volume is ≤0.034mol/L, or the total wt% concentration of soluble sodium salts, potassium salts, and magnesium salts contained therein is ≤0.20% (wt%), or the soluble sodium salts, potassium salts, and magnesium salts contained therein are ≤0.20% (wt%). The difference between the total concentration of potassium salt and magnesium salt and the total concentration of soluble sodium salt, potassium salt and magnesium salt in the water source taken from the production site is ≤0.01% (wt%); the weight ratio of auxiliary product E to main product A Controlled within the range of product E/product A ≤ 100/100 ~ 300/100, that is, ≤ 100/100 or ≤ 300/100;

Example 7-3. The preparation method of "auxiliary product F - fermented feed product" described in Example 1, which is at least characterized in that: the "by-product material 1: hot water delignification/ "Brown/black liquor discharged from the resin process" or/and "or by-product material 2: The fresh juice obtained by squeezing the fresh energy grass will be mixed with the energy grass that has only been broken/crushed, and then fermented to obtain auxiliary materials Product F;

Example 7-4. The preparation method of "auxiliary product G - pellet feed product" described in Example 1 is at least characterized in that: when using dry energy grass that has not been pressed as the starting main raw material, sieved The remaining materials after using the raw materials for the main product A are "fine powder passed through a 28 mesh sieve", or/and "energy grass fiber powder with a small soil content and a medium particle size passed through a 28 to less than 150 mesh sieve", as Ingredients in pellet feed products;

Example 7-5. The preparation method of "auxiliary product H--biomass pellet fuel product" described in Example 1 is at least characterized in that: the energy grass is crushed and sieved to remove crude fibers that have not passed the 28-mesh sieve. Fine powder, or full-component energy grass pulverization as ingredients, or biomass pellet fuel products added with waste plastics; the "waste plastics" include at least waste agricultural plastic films and waste foam Any one or more combinations of plastics, waste chemical fiber fabrics or/and chemical fiber wadding, the "addition" mentioned above accounts for less than 5% of the total weight of the auxiliary product H, or can be as high as no more than 22%;

Example 7-6. The preparation method of "auxiliary product I - edible fungus planting stick/block product" described in Example 1 is at least characterized in that: when energy grass, or energy grass and cow dung are used as the starting main raw materials, The remaining material after sifting out the raw materials for the main product A is the energy grass powder or fine cow dung sediment that has passed through a 28-mesh sieve, and is used as an ingredient in the edible fungus planting stick/block product.

Embodiment 8. For the equipment used in the "preparation method" described in Embodiments 4 to 7, please refer to Figure 14 - a block diagram of the flow of process equipment used in the production method of the product set of the present invention. It is also characterized by the following Examples 8-1 to 8-4 or as described in Example 8-5:

Example 8-1. Implementing "Step 1" to "Step 10" described in Example 4 involves setting up combined machinery I to X. Please refer to the δ block surrounded by "·-" in Figure 14, which includes:

The combined machine Ⅰ for the "pretreatment and preparation" of "Step 1" described in Embodiment 4, which at least includes: a crushing machine 1, any one or more combination crushers 2 of saw/mill/cut/hammer, Air separation machinery 3 and mechanical screening 4 are used to process the energy straw bundles through any one or more combinations of crushers, saws/mills/cuts/hammers, and then through air selection and screening. Take out the elongated fiber bundles with any mesh size ranging from 3 mesh to no more than 28 mesh in the energy grass crushed material; or set up the expansion machine 5 after the mechanical screen 4 to realize the obtained The slender fiber bundle energy grass crumbs after removal of impurities, purification and screening are then subjected to mechanical expansion treatment; thus, the mechanical settings of 1, 2, 3, 4, and 5 realize the "preparation" of step one in Example 4. Realization of "Processing and Preparing Materials" - Obtaining backup energy grass crumbs that can be processed in step 2;

The combined machine II for the "first batching" of the "Step 2" described in Embodiment 4 at least includes: a batching bin 6 for placing the "backup energy grass crumbs", containing the "first batching" described in the subsequent Step 7. A liquid tank 7 for the extruded water obtained from "secondary solid-liquid separation", or a bin 8 for storing "surfactant", a weighing scale 9, and a mixing and stirring device after the "first batching" Device 10; with this mechanical arrangement of 6, 7, 8, 9, and 10, the "first batching" of step 2 in Example 4 is realized;

The combined machine III for "heating dissolution" of "Step 3" described in Embodiment 4, which at least includes: a tank 11 for stirring, mixing, heating and insulation; with the mechanical setting of 11, the steps in Embodiment 3 are realized. "Natural dry material of 'Standby Energy Grass Crushed Material' material as described in the third step: 100 parts by weight", "Extruded water obtained from the 'second solid-liquid separation' described in the subsequent step seven": "2x parts by weight" , or with "0.1 to 0.3% by weight of 'surfactant' of 'extruded water' '2x parts by weight'", place these materials in a tank 11 that can be stirred, mixed, heated and insulated, and the materials Implement uniform stirring and heating to above 70°C, and keep warm;

The combined machinery IV for the "first solid-liquid separation" of "Step 4" described in Embodiment 4 at least includes: a conveying machine 12, a screw or roller squeezer 13, and a solid-liquid separator 14, Storage tank 15 for storing the "pressed/extruded brown/black liquor" obtained from the "first solid-liquid separation"; with the mechanical settings of 12, 13, 14, and 15, the steps described in step 4 of Example 4 are realized. "The material after heating and heat preservation operations is introduced into a screw or roller extruder, and the fiber bundles of the material are mechanically kneaded by crushing and extrusion, and then the material is introduced into a solid-liquid separator for solid/liquid separation." Or directly introduce the materials after the above heating and heat preservation operations into the solid-liquid separator for solid/liquid separation”;

The combined machine V for the "second batching" of the "step five" described in Example 4 at least includes: a storage bin 16 for placing the "moist material of the hydrophilic decomposable fiber intermediate product A to be processed". A liquid tank 17 containing the extruded water obtained from the "third solid-liquid separation" described in the subsequent step ten, or a silo 18 for storing "whisker additives", a weighing scale 19, and a "whisker additive" The mixing stirrer 20 after "the second batching"; thus, the mechanical settings of 16, 17, 18, 19, and 20 realize the mechanized operation of "Step 5" in Embodiment 4;

The combined machine VI for "grinding and latent elimination" of "Step 6" described in Embodiment 4, which at least includes: setting up a high-consistency refiner 21, and setting a to-be-processed machine in front of the feed port of the high-consistency refiner 21 The material storage bin 22 is provided with a conveying mechanism or conveying machinery 23 between the storage bin 22 and the high-consistency refiner 21; after the outlet of the high-consistency refiner 21, a heat preservation or heating function is provided The submersion elimination tank 24 is provided with a conveying mechanism or conveying machinery 25 between the outlet of the high-consistency refiner 21 and the feed inlet of the submersion elimination tank 24; thus, the machinery of 21, 22, 23, 24, 25 Set up to realize the mechanized operation of "Step 6" in Embodiment 4;

The combined machinery VII for the "second solid-liquid separation" of "Step 7" in Embodiment 4 at least includes: a conveying machine 26, a screw or roller squeezer 27, and a solid-liquid separator 28, The storage tank 19 for storing the "extruded water obtained from the 'second solid-liquid separation'" described in Step 7 of Example 3; thus the mechanical settings of 26, 27, and 28 realize the "Step Seven" of Example 4 mechanized operation;

Use the combined machine VIII for the "third batching" of "Step 8" described in Example 4, which at least includes: setting up and storing the moisture of the "hydrophilic decomposable fiber intermediate product B to be treated" described in Step 7 of Example 4. Material storage bin 29, a storage tank 30 for measuring and storing new water and circulating purified water, a bin 31 for storing whisker additives, a weighing scale 32, and a mixing tank 33; thus 29, 30, 31, 32 , the mechanical setting of 33 realizes the mechanized operation of "Step 8" in Embodiment 4;

The combined machine IX for "stirring and washing" of "Step 9" described in Embodiment 4 at least includes: a conveying mechanism or conveying machine 34, screw or roller extruder is provided after the aforementioned "stirring and mixing tank 33" Pulp machine 35, material temporary storage tank 36; from this, the mechanical settings of 34, 35, 36 realize the process purpose described in step nine in Example 4: introduce the "'third batching'" into the screw or roller squeezer , the fiber bundles of the material are mechanically kneaded by crushing and extrusion, and then the material is introduced into the temporary storage tank for the material to be finally squeezed dry; or the above-mentioned 'third batching' is directly introduced into the mixer for mixing, so that the new water and The old water originally contained in the moisture solid phase fiber of the hydrophilic decomposable fiber intermediate product B is fully mixed, and then Introduce the material into the temporary storage tank for the material to be finally squeezed out";

The combined machine X for the "third solid-liquid separation or final modification" of "Step 10" described in Embodiment 4, which at least includes: a conveying mechanism or conveying machine 37, a solid-liquid separator 38, and a storage cover The trough 39 for iron/manganese ion additives and the trough 40 for storing anti-mildew additives; with the mechanical arrangement of 37, 38, 39, and 40, the purpose of the process described in step ten in Example 3 is achieved: to obtain the results as shown in Example 3 "The extruded water obtained from the 'third solid-liquid separation'" described in step five of 4, and the final product - the main product of hydrophilic and decomposable fiber A including A-1 or/and A-2; or and do final touches to reduce product discoloration and mildew;

Example 8-2. The equipment used in implementing the "joint production method" described in Example 5 involves setting up combined machinery XI to XIII. Please refer to XI in the ε block surrounded by "·-" in Figure 14. to XIII, including:

The combined machinery XI used in the "co-production of A and C-1" described in Example 5-1 and Example 5-2 in Example 5 includes at least: the specific preparation method described in Example 5-1 in Example 5. Method, set up operating machinery 41 for removing roots and leaves of fresh energy grass, set up cleaning machinery 42 for washing, dehydrating and drying fresh energy grass, and set up "fresh energy grass after washing with water" The press 43 for squeezing and extracting juice from "grass" is equipped with a storage tank 44 for storing the fresh juice of the grass, which is the energy source of the squeeze, or a distillation kettle 45 for heating the fresh juice to boiling or evaporation and concentration, and a cooling and canning machine 46; Through the settings 41, 42, 43, 44, 45, and 46, it is possible to extract juice from fresh energy grass by removing roots, removing leaves, washing, dehydrating, pressing, and then heating and sterilizing, evaporating and thickening, cooling, and filling. , or mechanical treatment until it is heated and evaporated to dryness, to obtain edible or medical grade lignin/resin mixture by-product C-1, which can be in the form of a paste-like tan colloid, or a coffee-colored powder or granule, or a rosin-like solid block;

And for the specific production method described in Example 5-2 in Embodiment 5, an operating machine 47 for removing roots and blades of dry energy grass is provided, or a combined machine for crushing and screening the dry energy grass material is provided. 48. Set up a cleaning machine 49 for washing and dehydrating the dry energy grass. Set up a combined machine 50 that can add water, heat it to boiling, and then extract the juice. Set up a storage tank 51 for storing the squeezed energy grass juice. , the "energy grass juice" is also the by-product material 2 described in item ii of Example 2 - "the juice obtained by washing the dry energy grass with water and then boiling and pressing it"; or it can be set again The "energy grass juice" is heated to boiling or evaporated to concentrate the distillation kettle 52, and a cooling and canning machine 53 is installed; through the 47, 48, 49, 50, 51, 52, 53 set up here, the energy grass is dried, After removing roots, removing leaves, crushing, sifting, washing, dehydrating, soaking in hot water, pressing to extract juice, and then heating and sterilizing, evaporating and thickening, cooling, filling, or mechanical processing until heating and evaporation to dryness, the product can be obtained. Edible or medical grade lignin/resin mixture by-product C-1 in the form of pasta-like tan colloid, coffee-colored powder or granules, or rosin-like solid block;

The combined machinery XII used in the "coproduction of A and C-2" described in Examples 5-3 to 5-5 in Example 5, at least includes: the specific preparation method described in Example 5-3 in Example 5. Method, set up an operating machine 54 for removing roots and stripping leaves of fresh energy grass, set up a press 55 for pressing and extracting juice from fresh energy grass, set up a storage tank 56 for storing the fresh juice of pressed energy grass, or set up another The fresh juice is heated to boiling or evaporated and concentrated in the distillation kettle 57, and cooling and canning machinery 58 are set up; through the 54, 55, 56, 57, 58 set up here, the fresh juice can be obtained from the fresh juice through root removal, leaf removal, Press and extract the juice, then heat and sterilize, evaporate and concentrate, cool, fill, or mechanically process until it is heated and evaporated to dryness to obtain a tan colloid in the form of a paste, or a coffee-colored powder or granule, or a rosin-like solid. Feed or industrial grade lignin/resin mixture product C-2 in block form;

For the specific preparation method described in Example 5-4 in Embodiment 5, an operating machine 59 for removing roots and blades from the dry energy grass is provided, or a combined machine 60 for crushing and screening the dry energy grass material is provided. , is provided with a combined machine 61 that can add water, heat to boiling, and then perform juice extraction, and is provided with a storage tank 62 for storing the squeezed energy grass juice. The "energy grass juice" is also the item ii in Embodiment 2. The above-mentioned by-product material 1--the brown/black liquor discharged from the hot water delignification/resin process; or a distillation kettle 63 for heating the "energy grass juice" to boiling or evaporation and concentration, and cooling and canning is provided. Mechanical 64; through the 59, 60, 61, 62, 63, 64 set up here, it is possible to extract the juice from dry energy grass through root removal, leaf removal, crushing, sieving, hot water soaking, pressing, and then heating and sterilization. Evaporation and concentration, cooling, filling, or mechanical processing until heating and evaporation to dryness are used to obtain edible or medical grade lignin that can be in the form of a paste-like brown colloid, or a coffee-colored powder or granule, or a rosin-like solid block. /resin mix Compound by-product C-2;

In view of the specific preparation method described in Example 5-5 in Embodiment 5, a storage tank 65 is provided for storing the dewatered water after "cleaning" the energy grass in the combined machine XI, and a storage tank 65 is provided. A combined machine 66 for washing and screening cow dung with outflow water, a combined machine 67 for adding water, heating to boiling, and then squeezing, and a storage tank 68 for storing the squeezed energy grass juice, are provided. The "energy grass juice" is also the by-product material 1 described in item ii of Example 2 - the brown/black liquor discharged from the hot water delignification/resin process; or the "energy grass juice" is heated to The distillation kettle 69 for boiling or evaporation concentration is equipped with cooling and canning machinery 70; through the 65, 66, 67, 68, 69, 70 set up here, the cow dung can be washed, screened, soaked in hot water, and pressed. Juice, then heated and sterilized, evaporated and concentrated, cooled, filled, or mechanically processed until heated and evaporated to dryness, to obtain a tan colloid in the form of a paste, or a coffee-colored powder or granules, or a rosin-like solid block. Food or medical grade lignin/resin mixture by-product C-2;

The combined machine XIII used in the details of "can be walked again" and "can be guided later" described in Example 5-6 of Embodiment 5 at least includes: setting up a classification collection bin 71 to collect the combined machine XI, Ⅻ The energy grass or cow dung exported is "pressed and dregs out"; a combined mixing and heating machine 72 is provided to bubble the aforementioned "pressed dregs" into a loose floss-like material with a solid content of 25%; Mechanical sieve 73 is used to sift out the elongated fiber bundles in the particle size classification or mixing range of the foamed material that have a size ranging from 3 mesh to no more than 28 mesh sieve holes; it is set to collect the particle size ranging from 3 mesh to no more than 28 mesh sieve holes. A collection bin 74 of "graded or mixed elongated fiber bundles"; a conveying mechanism 75 is provided to guide the materials in the collection bin 74 to the "storage bin 16" of the aforementioned "combined machine V", so that the materials can For the classification of the "moist material of the hydrophilic decomposed fiber intermediate product A to be treated after initially removing the water solute in the fiber" described in step 4, the operations of steps 5 to 10 in Example 4 can be followed. Finally, The hydrophilic decomposable fiber product A-1 or A-2 can be obtained; a collection tank 76 is provided to collect the "washing of cow dung" and "washing and sieving with water" described in Example 5-5 in Example 5. The produced water containing cow dung is the "by-product material 3: the washing/washing liquid produced by washing/washing cow dung" described in item ii in Example 2, and can subsequently be directed to be used as in Example 1. One of the ingredients of the above-mentioned "auxiliary product E--liquid organic soil conditioner";

Example 8-3. The equipment used to perform the "preparation method" of "B" described in Example 6 involves setting up sub-assembly machines XIV to XVII. Please refer to the area surrounded by "·-" in Figure 14 XIV to XVII in the block, including:

Set up the "material preparation" sub-assembly device XIV of Example 6-1 in Embodiment 6, which also includes: a mechanical screen 77, or a crushing machine 78 and a winnowing machine 79;

Set up the "ingredients" sub-assembly device XV of Example 6-2 in Example 6, which also includes: a weighing scale 80, respectively storing "wood" and "plastic" in the composition of the "wood-plastic composite recycled material coarse particles". ” and softener storage bin 81, and mixing tank 82 after metering and batching;

Set up the "granulation" sub-assembly device XVI of Example 6-3 in Example 6, which also includes: a conveying machine 83 and a coarse granulator 84;

Set up the "homogenizing mixing" and "weighing packaging" sub-assembly devices XVII of Examples 6-4 to 6-5 in Example 6, which further include: a homogenizing mixing machine 85 and a weighing and packaging machine 86;

Example 8-4. The equipment used to implement the "manufacturing method" of the "auxiliary products" described in Example 7 involves setting up sub-assembly machines XVIII to IIIII. Please refer to the η surrounded by "·-" in Figure 14. XVIII to IIIII in the block, including:

Set up the sub-assembly device XVIII used in the preparation method of Example 7-1 "auxiliary product D--solid organic soil conditioner" in Example 7, which is characterized in that: it includes a set of assembly devices 87 for preparing solid organic soil conditioner; When "energy grass, or energy grass and cow dung" are used as the starting main raw materials, the remaining materials after extracting the raw materials for making the main product A are used, which are energy grass powder or fine cattle that have passed through a 28-mesh sieve. Fecal sediment, used as an ingredient in "auxiliary product D" for technological purposes;

Set up the sub-assembly device XIX used in the preparation method of Example 7-2 "auxiliary product E--liquid organic soil conditioner product" in Example 7, which is characterized in that: it includes a set of assembly devices 88 for preparing liquid organic soil conditioner product ; To achieve the use of "by-product material 1" or/and "by-product material 3" described in item ii in Example 2 as an ingredient in "auxiliary product E" The purpose of the process;

Set up the sub-assembly device Ⅱ Ⅹ used in the preparation method of Example 7-3 "auxiliary product F--fermented feed" in Example 7, which is characterized in that: it includes a set of assembly devices 89 for preparing fermented feed products; to realize the use of Embodiment 2 The purpose of the process of adding "by-product material 1" or/and "or by-product material 2" mentioned in item ii to the energy grass that has only been broken/pulverized and then fermenting it to obtain auxiliary product F;

Set up the sub-assembly device II used in the preparation method of Example 7-4 "auxiliary product G--pellet feed" in Example 7, which is characterized in that: it includes a set of assembly devices 90 for preparing pellet feed products; to achieve sifting out The remaining materials after using the raw materials for the main product A are "fine powder passed through a 28 mesh sieve", or/and "energy grass fiber powder with a small soil content and a medium particle size passed through a 28 to less than 150 mesh sieve", The technological purpose as an ingredient in pellet feed products;

Set up the sub-assembly device II II used in the preparation method of Example 7-5 "auxiliary product H--biomass pellet fuel" in Example 7, which is characterized in that: it includes a set of assembly devices 91 for preparing biomass pellet fuel products; to achieve "The energy grass is crushed and sieved to remove the coarse fiber that has not passed the 28-mesh sieve to remove the fine powder, or the full-component energy grass crushing material is used as the ingredient, or waste plastic is added." The technological purpose of biomass pellet fuel products;

Set up the sub-assembly device II III used in the preparation method of Example 7-6 "auxiliary product H--biomass pellet fuel" in Example 7, which is characterized in that: it includes a set of assembly device 92 for preparing edible fungus planting rods/block products; In order to realize "using energy grass, or energy grass and cow dung as the starting main raw materials, the remaining material after sifting out the raw materials for the main product A is the energy grass powder or fine cow dung that has passed through a 28-mesh sieve. Fecal sediment, as an ingredient component in edible fungus planting sticks/block products” process purpose;

Example 8-5. Alternatively, each of the machine units 1 to 88 described in the previous Examples 8-1 to 8-4 can be arranged neatly into a standard container.

Example 9. Introducing a standard sample for comparison and various comparisons between this standard sample and hydrophilic decomposable fiber A. Please refer to the attached figures 9 to 12:

Figure 9 is a black and white photo of a dry mass standard sample. It is made of willow dung, commonly known as willow dung by orchid planting enthusiasts - beetle larvae or wood beetle moth larvae that eat the willow stems. The dung is screened in the laboratory to remove particles larger than Impurities of 3 mesh and finer than 28 mesh are boiled in water to eliminate enzymes, then dehydrated but still containing 75% moisture by hand, pressed tightly into a disposable plastic cup, poured out, and kept at room temperature. Obtained after natural drying, this standard sample is pinched or compared with the dry mass of the hydrophilic decomposable fiber A sample of the present invention, and it can be qualitatively determined that the hydrophilic decomposable fiber A of the present invention is different from the standard sample. The relative hardness of the sample, or the physical properties such as the intertwining and interlocking strength of the tested sample fibers, can then be used to see the practicability of the hydrophilic and decomposable fiber of the present invention. The color of the standard sample in Figure 9 is brown.

Figure 10 is the "standard sample" described in Figure 9, which is a black-and-white photo of the accumulation on the ground under a willow tree in nature. In the photo, the white on the grass and leaves at the base of the willow tree trunk is "willow dung", and its real color is brown.

The standard sample shown in Figures 9 to 11 above - commonly known as willow manure, is a typical fiber that has been digested and degraded by enzymes in the digestive tract of wood-eating insects that can decompose cellulose/resin nutrients in wood; in the industry Technical personnel can know that wood fiber can be enzymatically produced into pulp; the dry dough standard sample shown in Figure 9 only needs to use a wooden stick hammer such as that used in ancient papermaking to beat the moisture material of this standard sample to produce Using paper pulp, you can make ordinary kraft paper or rough paper for calligraphy that are commonly seen on the market.

Because the inventor is currently short of many quality inspections on product paper test pieces, he can use the standard sample as shown in Figure 9 to compare the hydrophilic decomposable fiber A of the present invention in an object-by-object manner. , giving the following qualitative conclusion compared with the standard sample:

As shown in Figure 3, the material hardness of the dry mass of hydrophilic and decomposable fiber A-1 is lower than that of the standard sample;

As shown in Figure 4, the material hardness of the dry mass of hydrophilic decomposable fiber A-2 is lower than that of the standard sample. After rubbing it with the standard sample for at least 10 times, comparing the amount of damage caused by the rubbing of the two samples, it can be seen that: Equivalent to the standard sample, or no more than 5% of the missing amount of the standard sample times.

The "comparison" can be observed with the naked eye as shown in Figure 12 - a black and white photo of the scrap material from the standard sample in Figure 9 and the sample in Figure 4. From Figure 12, it can be seen that the material is brown and long. The thick fibers are from the standard sample in Figure 9, and the short and thin gray-white fibers in the picture are from the sample in Figure 4. When rubbing, both contact surfaces should choose the smoother and tighter parts; for a better comparison, you can use a balance to The weight reduction method is used to measure the weight loss of the two by rubbing them against each other. Of course, for the standard sample in Figure 9, the fiber thickness and length and the compactness of the agglomeration can be closer to that of the tested sample, and the comparison results will be more accurate.

Furthermore, the inventor observed during the preparation of the standard sample that even if "willow dung" is used as the enzyme species, an enzyme that can decompose lignin/resin in the wood fiber can be produced, and then this enzyme preparation is used to process The "energy grass crushed material" proposed by the present invention can also achieve the same effect as the present invention in the production water involved without inorganic soluble salts in the water, but the reduction is as described in item ii of Example 2. The "brown/black liquor", its weight part W _{brown/black liquor} , and the weight part W _A of the absolute dry fiber containing no more than 15% water in the main product A is W _{brown/black liquor} /W _A " In terms of reduction, there is no feature superior to the present invention; and the process operation after inoculating the material with enzyme is obviously more troublesome than the present invention, and the softening and grinding operations of the fiber cannot be significantly reduced. .

The dry dough standard sample of Example 9 is used for quality inspection. If the technical solution proposed by the present invention is industrialized and market customers want to improve their standards, the fibers of the standard sample can be finely divided to make the standard sample The strength increases; if you want to lower the standard, you can increase the number of fallen chips to "not more than the number of chips dropped by the standard sample" after rubbing the tested sample and the standard sample at least 10 times. In order to identify the color difference of the scraps dropped when the sample to be tested is rubbed against the standard sample, the standard sample can also be dyed with blue ink and other color liquids. The shape of the mass of the standard sample and the sample to be tested can also break through the constraints of Figures 3, 4, and 9. However, when comparing dry mass materials by pinching and rubbing, it is more fair and reasonable to use the same or similar surface contact.

Embodiment 10. The uses of the "product" or/and "preparation method" or/and "equipment" described in embodiments 1 to 8, at least include any one or a combination of more of the following:

Example 10-1. The "Main Product A - Hydrophilic Decomposable Fiber" described in Examples 1 and 2 can be used at least to prepare seedling paper, corrugated paper, cardboard, or/and include egg trays and convenient dinner plates/ It can be used as an alternative material to partially or completely replace waste paper recycled pulp in paper molded products such as bowls, paper seedling pots/bowls, etc.; it can also be used as a new starting material for further processing, such as making bleached pulp; Or as raw material for preparing cellulose ether;

Example 10-2. The "by-product B - wood plastic composite recycled coarse particles" described in Examples 1 and 3 can be used at least as wood plastic particles to be modified or/and used for hot extrusion of wood plastic products. Refined raw materials, or directly used as a new formulation raw material for hot-extruded wood-plastic products, or as a granular fuel for heating;

Example 10-3. The "by-product C-1 - edible or medical grade lignin/resin mixture" described in Example 1 can be used at least as a raw material for preparing beverages or/and traditional Chinese medicine preparations;

Example 10-4. The "by-product C-2--feed or industrial grade lignin/resin mixture" described in Example 1 can be used at least as a feed raw material, or/and as a water-reducing agent for concrete. Any softener in rubber/plastic;

Example 10-5. The "products", "preparation methods" and "equipment" described in Examples 1 to 8 can at least be used to prepare the "raw materials" described in Item 1 of Technical Solution 2 including Giant Juncao, etc. "Processing; or be expanded to the processing of bamboo, sugar cane bark, palm oil fruit bunch branches, etc.;

Example 10-6. The "products", "production methods" and "equipment" described in Examples 1 to 8 can all become independent commodities.

Embodiment 11. The business operation model of the "product" or/and "preparation method" described in any one or more of Embodiments 1 to 9, at least including any one or a combination of the following:

Example 11-1. A company can independently implement the commercial operations of “products” or/and “manufacturing methods”;

Example 11-2. Multiple companies can divide "product" varieties, or/and segment "manufacturing" processes to collaboratively implement commercial operations;

Example 11-3. The business model of self-operated or outsourced manufacturing can be used to implement the commercial operation of "products" or/and "manufacturing methods";

Example 10-4. The commercial operation described in Example 10-4 uses agricultural products including solid/liquid organic soil conditioners, and barters energy grasses including straw from grain, cotton and oil fields with farmers or farming operators.

The positive significance of the present invention is at least:

The present invention provides a collection of cleaning products and a manufacturing method using energy grass as raw materials. There are at least two core innovations therein: first, a collection of cleaning products is proposed. The "product collection" consists of main product A, Or the main product A is combined with any one or two of the by-products B and C, or the main product A is combined with the by-product B/C, and then is combined with any of the auxiliary products D, E, F, G, H, and I. It consists of a combination of one or more products; secondly, it provides a method for making the proposed "product set".

The positive meaning contained in the main product A of the present invention is at least that: some grain, cotton, oil and other crops that produce huge amounts of straw or branches are also classified into the upper code name of energy grass, and then all use energy grass as the upper code name. Name, the introduction is based on the aforementioned "energy grass, or energy grass and cow dung", which are crushed by any or more combinations of sawing/milling/cutting/hammering and then sieved to obtain the range of "passing 3 mesh to not passing 28 mesh" The slender fiber bundles of any mesh size are classified or mixed with particle sizes, and the main product A-hydrophilic decomposable fiber is prepared through cleaning. The ratio of the weight part W _{brown / black liquor of the brown / black liquor} discharged during the preparation process to the weight part W _A of the absolute dry fiber containing no more than 15% water in the main product A is W _{brown / black liquor} / W _A =90~100~300/100 range, and the ratio of the gram moles of Na ⁺ or/and K ⁺ or/and Mg ²⁺ contained in the "brown/black liquor" to the liter volume of the water contained in it is ≤0.034 mol/ L, its pH value does not exceed the range of 5.0 to 9.4, and all indicators do not enter the range of characteristic values of saline-alkali soil; the additives used include caustic alkali, ammonia, ammonium salts, peroxides, and biological enzymes. The total content of one or more species is 0. This is the green utilization of “brown/black liquor” resources that contain no more than 3 tons of dissolved salt and are harmless to vegetation per ton of main product A, and leads to the green utilization of “brown/black liquor” resources in this industry. siltation bottleneck.

The "product set" provided by the present invention surrounds the main product A - hydrophilic decomposable fiber, and sets two strains of by-products B, C, or/and auxiliary products D, E, F, G, H, and I. Combination walls. The positive significance of this "strain combination wall" is that around the core main product A, two lines of defense are set up to absorb various "waste" discharged in the process of preparing A, and can jointly integrate the main production Miscellaneous plastic waste and/or livestock and poultry manure surrounding the implementation site of Product A are also captured and collaboratively used for green resource utilization.

The main product A of the present invention has a small amount of “brown/black liquor” discharged during the production process and is harmless to vegetation, which makes it possible for the industrial implementation of the present invention to be carried out in areas near fields; Since it can be implemented near field areas, it also brings the possibility of obtaining energy grass materials with low transportation costs, including grain, cotton, and oil field straw. This also includes the use of auxiliary products D-solid organic soil improvement. The agent, or/and the auxiliary product E-liquid organic soil conditioner, can also be used to obtain energy grass materials such as straw and other energy grass materials through barter with farmers nearby at low cost. The described "'Brown/Black Liquor' amount is small and harmless to vegetation", "Use auxiliary product D, or/and auxiliary product E", "Obtain straw and other energy grasses through barter commercial exchange model with farmers in nearby fields. "Materials", this serial implementation can actually mean a breakthrough in the price barrier of farmers in our country's field fields being unable to compensate for the high price of organic fertilizers but slower effectiveness than inorganic fertilizers. After leaving the field, the straw is used in a circle and then turned into a liquid/solid organic soil conditioner, which also includes the consumption of livestock and poultry manure, etc., and is returned to the field without hindrance, which removes the air from the soil. Carbon dioxide is fixed into the straw by grain, cotton, and oil crops, and the straw is made into a collection of products A, B, C, D, E, F, G, H, and I, and finally is buried in the field without hindrance. But it is a good way to solve the problem of field failure year after year due to only applying organic fertilizer for many years. If this method is used to plant sea rice and giant rice in saline-alkali land, the saline-alkali land that is seriously lacking in organic matter will mature faster and become fertile land.

As described in Example 5 of the "Co-production method of 'main product A--hydrophilic decomposable fiber product' and 'by-product C--lignin/resin mixture product'", from an innovative perspective, the method used in this example The by-product C-1 obtained is a type a-1 technological innovation, which is a type of technological innovation such as the use of Juicyrus gigantea stalks to squeeze juice into beverages. raw material products for application; from a practical point of view, it can save the downstream enterprises of various uses from having to develop raw materials. All the troubles of starting a product.

When "by-product B - wood-plastic composite regenerated coarse particles" is introduced into the product collection, as introduced in Examples 1 and 6. Its innovation lies in the fact that in the field of raw materials for wood-plastic composite products, it has introduced a new raw material product dosage form of "coarse grain" that is not well known in this industry and its new preparation method. Its practicality lies in: first processing the foamed "wood" and "plastic" into coarse particles with low energy consumption. This coarse particles can be directly used in high-torque and low-speed screw extruders used in downstream wood-plastic composite products. , it can also be more conveniently fed into the grinding and regeneration process device described in the CN202010141136. The required homogenized quality of wood-plastic pellets is required, thereby bypassing the technological obstacle of the difficulty in directly feeding the foam-like "wood" and "plastic" into the screw extruder used for plastic granulation; the proposed coarse material contains "wood" or "plastic" The variable blending and application of the upper and lower limits of "plastic" reconciles the contradiction between the simplified production of the upstream and the variable content requirements of the downstream. Using "wood" from energy grass, the mechanical energy required for crushing is always lower than crushing from large pieces of waste wood, so this kind of "wood" has an energy-saving competitive advantage.

It is also worth mentioning that at least in the above-mentioned embodiments 1, 5, 7, and 8, it is mentioned that cow dung is used, and at least in the above-mentioned embodiments 1, 3, 6, 7, and 8, it is mentioned that waste Plastics are used, which once again elaborates on the realization of the concept of the invention at the level of specific implementation, that is: "The 'clean production method' not only requires self-cleaning of the snow in front of the door, but also the waste generated during the comprehensive utilization of energy grass. All resources such as liquids and liquids must be used for green utilization; the frost on other people’s tiles must also be taken away, and wastes such as cow dung around the implementation site or discarded agricultural mulch films in the fields must also be absorbed and used for green utilization.”

It can be mentioned again that when the low-level plants of energy grasses, which are fast-growing, tall plants and can tolerate fertilizer and water consumption, such as giant mushroom grass that cattle and others like to eat, are used as raw materials, then the Examples 5-5 in Example 5 are used. The technical solutions mentioned are implemented: "The washing/washing liquid discharged after the washing/washing of cow dung" "can be used as direct irrigation water for fertilizer-resistant and water-consuming giant fungus grass, etc."; its positive The meaning is to establish an environmentally friendly cycle chain: Giant Juncao comes from the "Giant Juncao planting plot"... Giant Juncao is derived from the "washing liquid" of cow dung, and then returns to this "Giant Juncao" The circular chain of "planting plots"; this circular chain not only makes the giant fungus planted on barren land become more lush, but also makes the land quickly turn from barren to fertile. On the basis of the cattle raising industry brought about by the Juncao planting industry, more subsequent utilization and processing industries of Juncao and their benefits have been added in a green way; this will make many barren wastelands in our country less likely to grow giant Juncao. The grass quickly becomes fertile soil with multiple benefits.

Of course, those skilled in the art will also make many modifications and improvements to the embodiments of the present invention, but these do not break through the equivalent changes and modifications of the embodiments of the concept of the present invention and the broad framework of the technical solution. Finally, the embodiments of the present invention are obtained. The above-mentioned "cleaning product collection and preparation method using energy grass as raw material" should all fall within the protection scope of the present invention.

Note: Explanation of the meaning of optional conjunctions or symbols used in this manual and other documents:

The first type, that is, "or", uses the general sentence pattern: A or B, which means: choose one of the two types - A or B.

The second type, namely "or/and", uses the general sentence pattern: A or/and B, which means: choose any one from three types - A, B, A and B.

The third type, "/", has three meanings: one is to express the proportional relationship between two quantities, such as A/B=3/5=3:5, which means A is better than B; the other is "/" It is equivalent to "÷"; the third one has the same meaning as the second one mentioned above.

The fourth type, "or and", uses the general sentence pattern: A or and B, which means: choose any one from the two types - A, A and B; it is also equivalent to "A or then and B" B" or "A, or again and B".

The fifth type is "or again", which is equivalent to any expression of "or and", "or and again", "or again and".

Claims

A collection of clean products using energy grass as raw material, which is characterized by: using energy grass, or energy grass and cow dung as the starting main raw materials, through the series and parallel connection of processing sub-paths, the clean production process and combined equipment or device array are integrated, and finally A collection of cleaning products is prepared, and the "product collection" is specifically composed of main product A as described below, or a combination of main product A and any one or two of by-products B and C; or main product A or and by-product B/C, and then combined with any one or more of the auxiliary products D, E, F, G, H, and I:

The main product A - hydrophilic decomposable fiber, characterized by: using the aforementioned "energy grass, or energy grass and cow dung", crushed by any or more combinations of sawing/milling/cutting/hammering and then sieving to obtain the "Elongated fiber bundles of any mesh size that pass through a sieve ranging from 3 mesh to no more than 28 mesh" are used as raw materials; the brown/black liquor will be discharged during the preparation process, and the "brown/black liquor" will be discharged. The ratio of the weight part W brown/black liquor of "black liquor" to the weight part W A of the absolute dry fiber containing no more than 15% water in the main product A is W brown/black liquor /W A = 90~100~300 /100 range; and the ratio of the gram moles of Na + or/and K + or/and Mg 2+ contained in the "brown/black liquor" to the liter volume of the water contained is ≤0.034mol/L, and its pH value is within 5.0~9.4 range; the total content of any one or more of caustic alkali, ammonia, ammonium salts, peroxides, and biological enzymes in the additives used is 0; or the water-insoluble or poorly soluble substances used in the preparation To make a whisker additive, implement low-ash whisker grafting/coating on the fiber surface. The "whisker additive" added to 100 parts by weight of the absolutely dry fiber in the main product A is ≤ 1 to 3 ~5~9 parts by weight, either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight; the main product α - a hydrophilic decomposable fiber product, which cannot be removed after being put into water or stirred again floating surface;

The main product A can be subdivided into the main product A-1 - a hydrophilic decomposable fiber controlled to have a low hydrophilic beating degree of <16°SR, and the main product A-2 - controlled to be Hydrophilic and decomposable fiber with high hydrophilic beating degree ≥16°SR;

By-product B - wood-plastic composite regenerated coarse particles; characterized by: at least the above-mentioned "energy grass" is crushed by any one or more combinations of sawing/milling/cutting/hammering, and then screened. The other part: "Fine materials or/and crushed materials that pass through a 28-mesh sieve, or crushed materials that are mixed with coarse and fine materials that pass through a 3-mesh sieve", and then use them with "waste plastics" as raw materials, or mix them with those in A The above-mentioned "brown/black liquor" has a mass transfer connection and is pelletized using a biomass fuel pellet machine;

By-product C - lignin/resin mixture, characterized by: It is produced using the "brown/black liquor" mentioned in A as raw material. It is a hydrophilic liquid in the color of black brown at room temperature, or in the form of a paste-like brown or Nearly black colloid, or in the form of coffee or nearly black powder or granules, or in the form of rosin-like solid; the by-product C, which can be subdivided into by-product C-1 - edible or medical grade lignin/resin mixture, By-product C-2 - feed or industrial grade lignin/resin mixture;

Auxiliary product D - solid organic soil conditioner, characterized by: the remaining material after extracting "energy grass, or energy grass and cow dung" that does not pass the 28-mesh sieve to make the main product A. Energy grass powder or fine cow dung sediment is used as one of the ingredients in the solid organic soil conditioner;

Auxiliary product E - liquid organic soil conditioner, characterized by: utilizing the brown/black liquor discharged during the preparation of the hydrophilic decomposable fiber main product A, or/and utilizing the discharged liquid due to upgrading the main product A and by-product C Pressed liquid or/and washing liquid or/and elutriated liquid, products blended according to the soil requirements of the crops and fields to be applied; the "discharged pressed liquid or/and washing liquid or/and elutriated liquid" Or "brown/black liquor", with a pH value in the range of 5.0 to 9.4, and the ratio of the gram moles of Na + or/and K + or/and Mg 2+ contained in it to the liter volume of the water contained therein is ≤0.034 mol /L, or the total wt% concentration of the soluble sodium salt, potassium salt, and magnesium salt contained therein is ≤ 0.20% (wt%), or the total concentration of the soluble sodium salt, potassium salt, and magnesium salt contained therein is consistent with the production implementation The difference in the total concentration of soluble sodium salts, potassium salts, and magnesium salts in the water source taken from the local area is ≤0.01% (wt%); the weight ratio of auxiliary product E and main product A is controlled at W E /W A ≤500/ 100 or ≤ or 2000/100 ≤ or 3000/100 range;

Auxiliary product F - fermented feed, characterized by: the product is mixed with the "brown/black liquor" discharged during the preparation process of main product A;

Auxiliary product G - pellet feed, characterized by: the energy grass dry material is only crushed and sieved to obtain a fine powder that passes through a 28 mesh sieve, or/and a particle size with a small soil content that passes through a 28 to less than 150 mesh sieve. Centered energy grass fiber crumbs for use as pellet feed One of the ingredients of the material;

Auxiliary product H - biomass pellet fuel, characterized by: the fine powder obtained by crushing and sieving the energy grass to remove crude fibers that have not passed the 28 mesh sieve, or the full-component crushed energy grass as ingredients. components; or waste plastics are added; the "waste plastics" include at least any one or combination of waste agricultural plastic films, waste foam plastics, waste chemical fiber fabrics or/and chemical fiber cotton batting, and the "waste plastics" "Additional" accounts for less than 5% of the total weight of auxiliary product H, or does not exceed 22%;

Auxiliary product I - Edible fungus planting stick/block, characterized by: the remaining material after extracting the main product A from "energy grass, or energy grass and cow dung" with a mesh size of no more than 28 mesh, and passing through a 28 mesh sieve. The energy grass powder or fine cow dung sediment of the hole is used as one of the ingredients in the edible fungus planting sticks/blocks.
The characteristics of the "main product A - hydrophilic and decomposable fiber" according to claim 1 include at least the following ⅰ to ⅵ, or a combination with ⅶ:

ⅰ. Raw materials used: including Echinacea, Liba, lemongrass, Arundodis, reeds, reeds, zebra grass, elephant grass, king grass, king bamboo grass, giant fungus grass, five-jointed miscanthus, rice grass, purple elephant grass , dwarf elephant grass, red elephant grass, sweet elephant grass, grass shoots, grass sugarcane, pseudosorghum, sweet sorghum, Peter grass, Sudan grass, Taiwan sweet grass, Pennisetum alterniflora, Spartina alterniflora hybrid, American wolftail Energy grasses of any one or more combinations of grasses and hybrid pennisetum, grain, cotton, and oil crops that produce a large amount of straw - rice, wheat, corn, cotton, rape, soybeans, oil peony, oil peony, sunflower, Energy grass of any one or more combinations of castor straws, or any one or more combinations of willows, bamboo willows, poplars, mulberry trees, and wolfberry trees that are artificially planted in dwarfs and whose upper branches need to be pruned all year round. Grass; crushed by any one or more combinations of sawing/grinding/cutting/hammering and then sieved, a part of it is obtained: fine particles with any mesh size ranging from 3 mesh to no more than 28 mesh sieve or mixed particle size Fragments of long fiber bundles;

ⅱ. By-product materials: By-product material 1: Brown/black liquor discharged from the hot water delignification/resin process. When making the "A" mentioned above, dry materials will be used in the hot water delignification/resin process. , the brown/black liquor is discharged by pressing/squeezing; the "brown/black liquor" has a weight part W of the brown/black liquor and a weight part W of the absolute dry fiber containing no more than 15% water in the main product A obtained The ratio of A is in the range of W brown/black liquor /W A =90~100~300/100; the gram moles of Na + or/and K + or/and Mg 2+ contained in the "brown/black liquor" are equal to The volume ratio per liter is ≤0.034mol/L, or/and the total wt% concentration of the soluble inorganic sodium salts, potassium salts, and magnesium salts contained in the water is ≤0.20% (wt%), or the soluble inorganic salts and potassium salts contained in the water The difference between the total wt% concentration of salt and magnesium salt and the total concentration in the water source taken from the production site is ≤0.01% (wt%), and the pH value of the "brown/black liquor" is in the range of 5.0 to 9.4;

Or by-product material 2: fresh juice obtained from fresh energy grass or fresh energy grass washed with water and then squeezed; or juice obtained from dried energy grass washed with water and then boiled and squeezed;

Or and by-product material 3: using cow dung as the starting material, the washing/washing liquid discharged after washing/washing the cow dung;

Or and by-product material 4: use activated carbon and acidic clay to adsorb and decolorize impurities in the aforementioned "brown/black liquor", and purify circulating water to obtain the decolorized adsorption sludge; or use the aforementioned "brown/black liquor", The decolorized adsorption sludge is obtained by adding sulfuric acid dropwise to acidify until the pH value does not exceed 7.0, and using activated carbon or activated carbon and acid clay to purify circulating water;

Or and by-product material 5: decolorized precipitated sludge obtained by precipitation and purification of the aforementioned "brown/black liquor" or/and "washing liquor" using chemical or biochemical methods;

ⅲ. Residual color: Add the main product A into clean water, heat the product to 70°C and bubble it for 5 to 10 minutes, then squeeze out the clear liquid material that has not evaporated and lost weight. The color of the color tube intuitively or the colorimeter detects is not thicker than the color of the "brown/black liquid" mentioned in item ⅱ diluted 16 times with clean water, or the instrument detects that its COD or BOD value is not higher than the "brown/black liquor" mentioned in item ⅱ The COD or BOD value of the "black liquor" diluted 16 times by the volume of clean water, or the discoloration consumption value of potassium permanganate measured by volumetric titration is not higher than the value of the "brown/black liquor" diluted 16 times by the volume of clean water as described in item ⅱ Potassium permanganate fading consumption value;

ⅳ. Product dosage form: The dosage form of the main product A can be a loose meat floss-like moist material with a water content of not more than 75%, a wet paper-like material with a water content of not more than 75%, a dry meat floss-like material with a water content of not more than 20%, and a water-based material. Any of paper-like dry materials containing no more than 20% water, compacted brick-shaped dry materials containing no more than 20% water, and compacted granular dry materials containing no more than 20% water;

ⅴ. Physical properties: Main product A-1 controlled to have a low hydrophilicity with a beating degree of <16°SR, or A-1 and main product A-2, A controlled to have a high hydrophilicity with a beating degree of ≥16°SR. -1 and A-2 are two sets of materials that can be blended easily and arbitrarily; they are compared with the standard sample pellets - the excrement of beetle larvae or wood moth larvae eating willow stems. In the pinch test of the material, the hardness of A-1 or A-2 ≤ the hardness of the standard sample; or in the test of rubbing the dough with the standard sample for at least 10 times, it can be seen with the naked eye or Use a balance to weigh and compare, the amount of scattered chips of A-1 or A-2 is not more than 5 times the amount of scattered chips of the standard sample;

ⅵ. Production process characteristics: During the production process, the ratio of the gram moles of Na + or/and K + or/and Mg 2+ contained in the water involved to the liter volume of "water" is ≤0.034 mol/L; and adopt Impregnate the fiber material with water of not less than 70°C at least twice to remove the lignin/resin in the fiber; the flow direction of the gradually thickening brown/black liquor in the "water" flow is consistent with the flow direction of the fiber material in the production process The flow direction in the product is countercurrent; or water-insoluble or poorly soluble substances are added as whisker additives, and the amount added is ≤1~3~5~9 parts by weight for 100 parts by weight of absolute dry fiber in the main product A or its intermediate product parts by weight, either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight, implement low-ash whisker grafting/coating on the fiber surface; among the additives used, caustic alkali, ammonia The total content of any one or more of ammonium salts, peroxides, and biological enzymes is 0;

ⅶ. Preferable parameters: or "The ratio of the discharged weight part W brown/black liquor and the total obtained weight part W A of the absolutely dry main product A with a water content not exceeding 15% as described in item ⅱ is W brown/black Liquid /W A = 100~120~150/100 range; or "adding water-insoluble or poorly soluble substances as whisker additives as described in item ⅵ, the amount added is equivalent to the absolute dry fiber in the main product A or its intermediate product "100 parts by weight""is ≤1~3~5 parts by weight", "either ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight"; the "whisker additive" is at least a saturated aqueous solution of calcium hydroxide , any kind of silica sol, or/and newly generated calcium hydroxide, aluminum hydroxide, hydrated silicic acid, calcium silicate, magnesium silicate, aluminum silicate, calcium carbonate, calcium sulfate dihydrate, Any one or more combinations of ferric hydroxide, or/and any one or more of kaolin, clay, fly ash, wollastonite that has been ultrafinely pulverized to the point where it cannot naturally precipitate to clear surface water within half an hour in water. A combination of these, or a combination of any one or more of kaolin, clay, fly ash, and wollastonite crushed to over 320 mesh.
The "by-product B - wood-plastic composite regenerated coarse particles" described in claim 1 is more characterized in that: the characteristics of "wood" are as follows 3-1 or the combination of 3-1 and 3-2, wherein "plastic "The characteristics are the following 3-3 or the combination of 3-3 and 3-4, and the product dosage form characteristics are the following 3-5 to 3-8:

3-1. The “wood” includes part of the energy grass: fine materials or/and crushed materials that pass through a 28-mesh sieve, or crushed materials mixed with coarse and fine materials that pass through a 3-mesh sieve;

3-2. The "part" as described in 3-1 above is the dry basis weight of the "wood" containing 15% of equilibrium water after natural drying in the air, accounting for 5% to 5% of the total weight of by-product B. Between 78% (wt%);

3-3. The raw materials for "plastic" are all selected from waste plastics;

3-4. "Waste plastics" as described in 3-3 above, at least include any one or a combination of more as described below: Miscellaneous waste plastic film residue discarded from waste paper recycling, including the "miscellaneous waste plastic film" "Residue" obtained by water flotation, floating plastics or/and submerged plastics; plastic film waste packaging bags for commodities, cut/punch edges from the production of plastic film packaging bags, waste composite plastic film materials, trademarks Plastic film composite release paper/film, waste aluminum-plastic composite film, and waste agricultural plastic film discarded during label production/use; impurity-containing polymer fibers separated from waste tires after crushing, waste removed from cars Chemical fiber flannel, waste chemical fiber carpet, waste chemical fiber fabric, waste chemical fiber meltblown cloth, waste chemical fiber filter paper; waste wire plastic skin, waste plastic packaging tape, waste plastic woven bag, waste geotextile, waste/old plastic shoes, waste plastic shop Ground products, waste plastic toys, waste plastic barrels, waste plastic bottles, waste plastic geotextiles, waste/old plastic lawns, waste plastic building materials, waste plastic pipes, waste plastic boards, waste plastic stationery, waste plastic boxes/bags, waste Miscellaneous plastic parts; waste PVC artificial leather, waste PU artificial leather; waste foam plastic;

3-5. The dosage form of by-product B can be at least set into the first group of A, B, C, and D, or/and the second group of E, Ji, Geng, and Xin, or/and the third group of Ren and Gui. , that is, any one or more of A to Gui in the first to third groups can be blended and combined in any ratio to easily make the downstream plastic particles or coarse particles of wood-plastic composite regeneration. "Wood" in products or The proportion of the total weight of "wood" carrying "impurities" ranges from 5% to 78%; the weight ratio of the two in the aforementioned "'wood' carrying 'impurities'" is W impurities /W wood = 0~10/ 100. The "wood" is absolutely dry material with a moisture content of no more than 15%, and the "impurities" are "by-product materials 4" or/and "by-products" as described in claim 2, ii. Material 5"; the total weight of "plastic" and softener is in the range of 22% to 95%. The weight ratio of the two in the aforementioned "'plastic' and softener" is W waste plastic /W softener = 100 /0～100:

First group:

The total weight input of "wood" in A includes 76%, and the total weight input of waste plastics and softeners accounts for 24%;

The total weight input of "wood" in B is 35%, and the total weight input of waste plastics and softeners is 65%;

The total weight input of "wood" in C is 25%, and the total weight input of waste plastics and softeners is 75%;

The total weight input of "wood" in D is 5, and the total weight input of waste plastics and softeners is 95%;

Second Group:

The total weight input of "wood" in E includes 77%, and the total weight input of waste plastics and softeners accounts for 23%;

The total weight input of "wood" accounts for 38%, and the total weight input of waste plastics and softeners accounts for 62%;

The update includes that the total weight input of "wood" accounts for 23%, and the total weight input of waste plastics and softeners accounts for 77%;

The total weight input of "wood" in Xin is 10, and the total weight input of waste plastics and softeners is 90%;

The third group:

The total weight input of "wood" in Renzhong accounts for 78%, and the total weight input of waste plastics and softeners accounts for 22%;

The total weight input of "wood" in Guizhong accounts for 15%, and the total weight input of waste plastics and softeners accounts for 85%;

3-6. Or as described in item 3-5, "select one or more of the A to Gui in the first to third groups and use them in combination to control the downstream coarse particles of the wood-plastic composite regenerated material. The total weight of "wood" in plastic particles or products is in the range of 5% to 78%, and the total weight of "plastic" and softener is in the range of 22% to 95%", items 3-5 The proportion of the total weight of "wood" in each feeding combination from A to Gui in the "first group", "second group" and "third group", and the proportion of the total weight of "plastic" and softener, All can be customized according to market customers;

3-7. The "wood-plastic composite recycled coarse particles" are composed of materials according to the "first group" or/and the "second group" or/and the "third group" mentioned in item 3-5. The ingredients from A to Gui are combined and fed. After being processed by a coarse granulator, the resulting texture is low-strength coarse granules that can be directly pulled/pulled/pinched/teared/grabbed with fingers/palms. The "low-strength coarse granules" "Strength", at least the standard sample specimen of plastic with tensile strength ≤3PMa;

3-8. The "coarse granulator" mentioned in item 3-7 above specifically refers to any feed pellet machine, organic fertilizer granulator, or biomass fuel pellet machine with continuous feeding/discharging function. , or a spiral granulator and intermediate crusher can be connected in series after the aforementioned "granulator"/"granulator".
The manufacturing method of "main product A - hydrophilic decomposable fiber product" in the product set described in claim 1 can be characterized by including the following steps one to ten:

Step 1 - Preprocessing and preparation:

Classify the energy grass dry materials first, or further remove impurities from metals or/and masonry blocks or/and bark impurities contained in the classified materials, and then classify and remove impurities. The energy grass is crushed by any one or more combinations of sawing/grinding/cutting/hammering and then screened; the crushed energy grass that passes through a 28-mesh sieve is discharged for further use;

Sieve out the elongated fiber bundles with classified or mixed particle sizes in any mesh range from 3 mesh to 28 mesh in the energy grass crushed material;

Or the slender fiber bundle energy grass crumbs that have been removed and purified are subjected to mechanical expansion processing;

Thus, the backup energy grass crumbs prepared for step 2 are obtained. This "backup energy grass crumbs" material is called natural absolutely dry material based on its naturally adsorbed equilibrium water content in the air of 15% (wt). ;

Step 2 - First Ingredients:

Take 100 parts by weight of the natural dry material of the "Standby Energy Grass Crushed Material" material obtained in step 1, and mix in the extruded water obtained from the "second solid-liquid separation" described in the subsequent step 7. "Put in" and "squeeze out water", and after measuring that the free water carried by 100 parts by weight of the natural absolutely dry material in the solid phase obtained in the "first solid-liquid separation" described in the subsequent step 4 is x parts by weight, then "mix "Put in" "extruded water" is no less than: 2x parts by weight; or mix in 0.1 to 0.3% by weight of the surfactant: sodium butyl naphthalene sulfonate of the "2x parts by weight" of the aforementioned "extruded water" , any one or more combinations of sodium dodecyl benzene sulfonate, sodium lauryl sulfate, or/and any one or more combinations of coconut oil fatty acid diethanolamide, fatty alcohol polyoxyethylene ether ; The "2x" corresponds to 100 parts by weight of the natural dry material of crushed energy grass materials: in the range of 25 to 50 to 300 parts by weight;

Step three - heating and dissolution:

Add the aforementioned "100 parts by weight of the natural dry material of 'Standby Energy Grass Crushed Material'" and "the squeezed water obtained from the 'second solid-liquid separation' described in the subsequent step seven": "2x parts by weight", or and "'Extruded water'" 2x parts by weight" and 0.1 to 0.3% by weight of 'surfactant'", place these materials in a tank that can be stirred, mixed, heated and insulated, and stir the materials evenly and heat to above 70°C, and keep it warm for at least 5 minutes, or take samples for analysis. When the color of the extruded liquid no longer changes to a darker color, you can stop this heating and heat preservation operation;

Step 4 - First solid-liquid separation:

The material after the above "heating and heat preservation operation" is introduced into a screw or roller extruder, and the fiber bundles of the material are mechanically kneaded by crushing and extrusion, and then the material is introduced into a solid-liquid separator for solid/liquid separation. ; Or directly introduce the material after the above-mentioned heating and heat preservation operations into a solid-liquid separator for solid/liquid separation; thereby obtaining the "pressed/extruded brown/black liquor" as claimed in claim 1, and the initial fiber removal The moisture material of the hydrophilic decomposable fiber intermediate product A to be treated with water solute;

In this "first solid-liquid separation", the "pressed/extruded brown/black liquor" obtained is naturally separated from the hydrophilic decomposable fiber intermediate product A by the weight portion of the discharged brown/black liquor. The proportion of dry material weight part W hydrophilic decomposable fiber intermediate product A can be controlled by using conventional solid-liquid separation machinery at W pressing/extrusion brown/black liquor /W hydrophilic decomposable fiber intermediate product A =25~100~ In the range of 300/100, in this "first solid-liquid separation", the weight percentage of the natural absolute dry material of the "hydrophilic and decomposable fiber intermediate product A" in the obtained moisture material can be controlled between 80% and 50%. 25% range;

Step 5 - Second batching:

After measuring that the free water carried by 100 parts by weight of the natural dry material in the solid phase of the "moist material of the hydrophilic decomposable fiber intermediate product A to be treated" described in step 4 is "Moist material of fiber intermediate product A" contains 100 parts by weight of natural absolutely dry material and x parts by weight of free water, and then mix in the extruded water obtained in the "third solid-liquid separation" described in the subsequent step ten. Not less than: "Whisker additive" is at least any one of calcium hydroxide saturated aqueous solution, silica sol, or/and newly generated calcium hydroxide, aluminum hydroxide, hydrated silicic acid, calcium silicate, magnesium silicate, Any one or combination of aluminum silicate, calcium carbonate, calcium sulfate dihydrate, ferric hydroxide, or/and kaolin, clay, etc. that have been ultrafinely crushed to the point where they cannot naturally precipitate to a clear surface within half an hour in water. Any one or more combinations of fly ash and wollastonite, or any one or more combinations of kaolin, clay, fly ash, and wollastonite crushed to over 320 mesh; the "whisker additive" ”, the added amount of 100 parts by weight of absolute dry fiber in the “moist material of hydrophilic decomposable fiber intermediate product A” is ≤1~3~5~9 parts by weight, that is, the added amount is ≤1 part by weight or ≤3 parts by weight parts or ≤5 parts by weight or ≤9 parts by weight;

Mix the second batching ingredients described in step 5 in the mixing tank first to form the materials to be processed by high-concentration grinding;

Step 6 - Grind to eliminate potential:

Introduce the "materials to be fed into the high-concentration grinding process" obtained in step 5 into the high-concentration grinding process; or then introduce the heat-generating materials from the high-concentration grinding into a latent elimination tank with a heat preservation setting for insulation or heating. Let it stand at a temperature of not less than 70°C to relax the kinks and curls in the fibers produced during the high-concentration grinding process, and to dissolve the hydrophobic lipids in the fibers;

After processing in step 6, the material after grinding or processing is obtained and is subject to solid-liquid separation;

Step 7 - Second solid-liquid separation:

The above-mentioned "material after grinding or processing" is introduced into a screw or roller extruder, and the fiber bundles of the material are mechanically kneaded by crushing and extrusion, and then the material is introduced into a solid-liquid separator for solid/liquid separator. Liquid separation; or omitting mechanical softening, the above-mentioned "materials after grinding or processing" are directly introduced into the solid-liquid separator for solid/liquid separation; thereby obtaining the "materials after grinding or processing" as described in the previous "Step 2" "The extruded water obtained from the 'second solid-liquid separation'" and the wet material of the hydrophilic and decomposable fiber intermediate product B are to be finally washed with new water;

Step 8 - The third ingredient:

After measuring that the free water carried by 100 parts by weight of the natural dry material in the solid phase of the "moist material of the hydrophilic decomposable fiber intermediate product B to be treated" described in step seven is The "moist material of fiber intermediate product B" contains 100 parts by weight of natural absolutely dry material and x parts by weight of free water, or may be combined with a whisker auxiliary, and the "whisker auxiliary" at least includes hydrogen Any one of calcium oxide saturated aqueous solution, silica sol, or/and any one of newly generated calcium hydroxide, aluminum hydroxide, and silica sol in the aqueous phase, or/and newly generated calcium hydroxide in the aqueous phase , aluminum hydroxide, hydrated silicic acid, calcium silicate, magnesium silicate, aluminum silicate, calcium carbonate, calcium sulfate dihydrate, iron hydroxide, any one or a combination thereof, or ultrafinely crushed into water Any one or combination of kaolin, clay, fly ash, and wollastonite that is difficult to naturally precipitate to a clear surface within half an hour, or kaolin, clay, fly ash, and wollastonite crushed to a mesh size of 320 Any one or a combination of more; the "whisker additive" added to 100 parts by weight of absolutely dry fiber in the "moist material of intermediate product B" is ≤1~3~5~9 parts by weight , that is, the addition amount is ≤1 part by weight or ≤3 parts by weight or ≤5 parts by weight or ≤9 parts by weight;

From the metered addition of water and whisker additives in step eight, the third ingredient to be sent to step nine is obtained;

Step 9 - Stir and wash:

Introduce the "third batching" of the above step 8 into the screw or roller squeezer, perform mechanical kneading treatment on the fiber bundles of the material, and then introduce the material into the temporary storage tank of the material to be finally squeezed dry. ; Or the above-mentioned "third batching" can be directly introduced into the mixer for stirring, so that new water, or the old water material originally contained in the moisture solid phase fiber of the whisker additive and the hydrophilic decomposable fiber intermediate product B can be achieved. Mix thoroughly, and then introduce the material into the temporary storage tank for the final squeezed dry material;

From the processing in step nine, the material to be finally squeezed out and sent to step ten is obtained;

Step 10 - The third solid-liquid separation or final modification:

Introduce the "material to be finally squeezed dry" in the above step nine into the solid-liquid separator for solid/liquid separation; thereby obtaining the extruded material obtained by the "'third solid-liquid separation'" as described in the previous "step five". "Water out", and the final product - including the hydrophilic decomposable fiber A product of A-1 or/and A-2; or adding additives that mask iron/manganese ions to the final product: oxalic acid, sodium oxalate, potassium oxalate , ammonium oxalate, ethylenediaminetetraacetic acid, sodium ethylenediaminetetraacetate, tetraacetylethylenediamine, citric acid, sodium citrate, tartaric acid, sodium tartrate, gluconic acid, diethylenetriaminepentaacetic acid, diethyleneethylene A combination material of any one or more of triamine pentamethylene phosphonic acid, pentasodium diethylene triamine pentaacetate, and sodium nitrilotriacetate. The combination material can be formulated into an aqueous masking aid solution: Combination The total molar amount of materials added is in the range of 0.1~1.2mol/L. The amount of masking additive aqueous solution can be controlled at 100 parts by weight of absolutely dry hydrophilic decomposable fiber A, and 1 to 2 parts by weight of masking additive aqueous solution; or and then Add conventional amounts of common antifungal additives to the final product.
The co-production method of "main product A - hydrophilic decomposable fiber product" and "by-product C - lignin/resin mixture product" in the product set as claimed in claim 1, has at least the following features: making A and C- 1 co-production, you can first go through the following steps 5-1 or/and 5-2; or make A and C-2 co-production, you can go through the following steps 5-3 or/and 5-4 or/and 5-5 first; In the end, it was achieved by taking 5-6 steps:

5-1. Use fresh energy grass to remove the whole plant with roots and leaves or peel off the stem parts of the leaves, wash it with clean water, dehydrate and dry it, and then press it into a juicer. It is better to control the pressing. The moisture content of the final slag is below 20% (wt%), and the liquid squeezed out It is the by-product material 2 described in item ii of claim 2 - "fresh juice obtained from fresh energy grass washed with water and then squeezed"; or this "fresh juice" is heated to 100-105 Keep at ℃ for 3 to 5 minutes, cool and can the liquid black brown edible or medical grade lignin/resin mixture product C-1; if it is heated at the same time, the "fresh juice" is evaporated and concentrated. Operation, under the control of process parameters that control the amount of steamed water, the steamed concentrated material of "fresh juice" can be in the form of a tan paste-like colloid, or a coffee-colored powder or granules when cooled to room temperature. Or edible or medical grade lignin/resin mixture product C-1 in the form of rosin-like solid blocks;

5-2. Use the energy grass that has been sun-dried or naturally dried or oven-dried to remove the whole plant with roots and leaves or remove the stem part of the leaves, or use the dry energy grass material to remove 28% by crushing and screening After sieving the coarse material into fine powder, wash it with clean water. You can add water ranging from 0.7 to 5.7 times the weight of the dry material, heat it to 70°C or even boil it, and then press it into a juicer. It is better to control the amount of water after squeezing. The moisture content of the residue is below 20% (wt%), and the liquid squeezed out is the by-product material 2 described in item ii of claim 2 - "dry energy grass washed with water and then boiled and pressed." "Obtained juice"; or heat this "juice" to 100-105°C for 3-5 minutes, cool it, and can it into a liquid black brown edible or medical grade lignin/resin mixture product C-1; If the "juice" is subjected to an evaporation and concentration operation while heating, then under the control of process parameters that control the amount of steamed water, the "juice" can be evaporated and concentrated, and then when cooled to room temperature, it can be presented as noodles. Edible or medical grade lignin/resin mixture product C-1 in the form of paste-like brown colloid, or coffee-colored powder or granules, or rosin-like solid block;

5-3. Use fresh energy grass wet material to remove the roots and leaves of the whole plant or remove the stem parts of the leaves, and then squeeze it into a juicer. It is better to control the moisture content of the residue after pressing to be 20 % (wt%) or less, the liquid squeezed out is the by-product material 2 described in item ii of claim 2 - "fresh energy grass" and "fresh juice obtained by pressing"; or the "fresh juice" "Heat to 100~105℃ and hold for 3~5 minutes, cool and can the liquid black brown feed or industrial grade lignin/resin mixture product C-2; if it is heated at the same time, then "fresh" "Juice" is subjected to an evaporation and concentration operation, and under the control of process parameters that control the amount of steamed water, the steamed and concentrated material of "fresh juice" can be in the form of a brown colloid like a pasta sauce when it is cooled to room temperature, or Feed or industrial grade lignin/resin mixture product C-2 in the form of brown powder or granules, or rosin-like solid blocks;

5-4. Use the whole plant with roots and leaves removed from the energy grass that has been sun-dried or naturally dried or oven-dried, or use the stem material with the leaves peeled off, or use the dry energy grass material only after crushing and screening. After passing through a 28-mesh sieve, the coarse material can be added with 0.7 to 5.7 times the weight of the dry material in water, heated to 70°C or even boiled, and then pressed in a juicer. It is better to control the moisture content of the residue after pressing. Below 20% (wt%), the liquid squeezed out is either the by-product material 1 described in item ii of claim 2 - brown/black liquor discharged from the hot water delignification/resin process; or the "brown liquor" /Black liquor" is heated to 100~105℃ for 3~5 minutes, cooled and canned to obtain a liquid black brown feed or industrial grade lignin/resin mixture product C-2; if it is heated at the same time, then The "brown/black liquor" is subjected to an evaporation and concentration operation, and under the control of process parameters that control the amount of steamed water, the "brown/black liquor" can be evaporated and concentrated, and then when cooled to room temperature, it can be turned into a pasta sauce The feed or industrial grade lignin/resin mixture product C-2 is in the form of brown colloid, or coffee-colored powder or granules, or rosin-like solid block;

5-5. Collect and remove the water after "washing with clean water" mentioned in item 5-1 or/and 5-2 above, use this water to wash the cow dung, remove impurities that pass through a 28-mesh sieve, and remove Obtain the crude fiber that has not passed 28 sieves after being washed with water, boil it to kill the cellulolytic enzymes in it, and then put it into a juicer for squeezing. It is better to control the output after squeezing. The moisture content of the slag is below 20% (wt%), and the liquid squeezed out is the by-product material 1 described in item ii of claim 2 - brown/black liquor discharged from the hot water delignification/resin process; or Heat the "brown/black liquor" to 100-105°C for 3-5 minutes, cool it, and can it to form a liquid black brown feed or industrial grade lignin/resin mixture product C-2; if it is heated At the same time, the "brown/black liquor" is subjected to an evaporation and concentration operation. Under the control process parameters of controlling the amount of steamed water, the "brown/black liquor" can be evaporated and concentrated and then cooled to room temperature. Feed or industrial grade lignin/resin mixture product C-2 in the form of a paste-like brown colloid, or coffee-colored powder or granules, or rosin-like solid block; it is discharged after washing/washing of cow dung If the washing/washing liquid is used, it can at least be used as direct irrigation water for planting the fertilizer-resistant and water-consuming giant Juniper grass;

5-6. The slag mentioned in the above 5-1 to 5-5 "It is better to control the moisture content of the slag after pressing to be below 20% (wt%)" can be soaked into a solid content of 25%. The loose floss-like material is sifted out and the elongated fiber bundles with particle size classification or mixing ranging from 3 mesh to no more than 28 mesh can be obtained. "The moisture material of the hydrophilic decomposable fiber intermediate product A to be treated to remove the water solute in the fiber" can be followed by the fifth to tenth steps in claim 4, and finally the hydrophilic decomposable fiber product A-1 or A-2; The water containing cow dung produced by "washing cow dung" and "washing and sieving with water" described in the aforementioned 5-5 is the "water containing cow dung" described in item ii of claim 2 By-product material 3: "washing liquid produced by washing cow dung" can be directed to be one of the ingredients of the "auxiliary product E - liquid organic soil conditioner" described in claim 1.
The preparation method of "B - wood-plastic composite recycled coarse-grained product" in the product set of claim 1 is characterized by the following 6-1 to 6-6:

6-1. Material preparation: For the slag described in any one of 5-1 to 5-5 in claim 5, "It is better to control the moisture content of the slag after pressing to be below 20% (wt%)", Prepare the "wood" material in "Wood Plastic Composite Regenerated Coarse Grains";

Or/and use dry energy grass that has not been pressed, and only crush or cut into sections once, then winnow or/and screen, and select materials with less nutrients to make "Wood-Plastic Composite Regenerated Coarse Grain" The "wood" is prepared, and the remaining materials with more nutrients are used as organic fertilizer or/and feed materials; the "materials with less nutrients", in terms of measurement, are the materials that have been crushed or cut into pieces after one Finally, the crude energy grass fiber that can withstand the mechanical crushing force without being more finely divided and passes through a sieve ranging from 3 to 28 mesh, and the fine energy grass that has a higher soil content in the crushed energy grass that passes through a 150 mesh sieve. Fiber powder; the "materials with more nutrients", in terms of measurement, are materials that cannot withstand the mechanical crushing force and are more finely crushed after being crushed or cut into pieces once, and pass through a sieve ranging from 28 to no more than 150 mesh. Energy grass fiber powder with small soil content and medium particle size;

Waste plastic raw materials purchased or/and collected for free, which are in a compressed and packaged state or/and which contain large pieces of metal or brick-like solids, must first be crushed and winnowed to loosen the materials. and remove hard solids such as metal and bricks; use the fluffy waste plastic with impurities removed as the "plastic" material in "wood-plastic composite recycled coarse particles";

6-2. Ingredients: According to the proportion of "wood", "plastic" and softener in the total weight of the product in the composition of the "wood-plastic composite regenerated coarse particles" described in 3-4 or 3-5 of claim 3. Ratio, weigh ingredients;

6-3. Granulation: The materials prepared by the scale are passed through the mixing and collecting bin, then transported by machinery, and put into the "coarse granulator" described in claim 3-7 and 3-8. Granules; the machinery used in the "coarse granulator" is: any of the feed pellet machine, organic fertilizer granulator, biomass fuel pellet machine with continuous inlet/output function, or any of the above-mentioned The "granulator"/"granulator" is then connected in series with a spiral granulator and intermediate crusher; the aforementioned "granulator"/"granulator" discharges the material in the form of segmented granules formed by the through-hole die. For example, the aforementioned "granulator"/"granulator" The "segmented granular" "materials" are then processed by the spiral granulator in series, and then the materials come out of the machine as irregular particles; the materials during granulation are heated by mechanical extrusion/friction, and can be used to feed the materials or /The water is added to the interlayer in the machine to control the outgoing material to not exceed 110°C; the "coarse wood-plastic composite recycled material" produced by this operation has a texture that can be directly pulled/pulled by human fingers/palms/ Low strength when kneaded/torn into pieces; its granulated shape at least includes segmented granules or irregular particles formed by a through-hole mold; the hole shape of the "hole mold" includes at least equilateral or unequal side lengths Any one of 3 to 12 sides, or round; the size of the "grain" is classified or mixed in any aperture ranging from 25mm to less than 2.0mm mesh;

6-4. Homogenization and mixing: If the "wood-plastic composite recycled coarse particles" obtained in item 6-3 have obvious quality defects such as inhomogeneous packaging after subsequent packaging, they can be added before weighing and packaging. Mixing and homogenizing treatment, the above-mentioned treatment is to use a mechanical roller to introduce the "wood-plastic composite recycled coarse particles" obtained in item 5-3, and tumble and mix evenly;

6-5. Weighing and packaging: The "wood-plastic composite recycled coarse particles" obtained in items 6-3 or/and 6-4 that meet the quality requirements are weighed and introduced into packaging bags with specifications approved by market customers;

6-6. Warehousing quality inspection: Put the packaged products into the warehouse in order, and give each batch according to the indicators that market customers need to know. Quality inspection reports of incoming products are archived.
The preparation method of "auxiliary products" D to I in the product set of claim 1 is characterized by the following: 7-1 to 7-6:

7-1. The preparation method of "auxiliary product D - solid organic soil conditioner product" according to claim 1, which is at least characterized in that: when using energy grass, or energy grass and cow dung as the starting main raw materials, use extracted The remaining materials after making the main product A, including energy grass powder or fine cow dung sediment that has passed through a 28-mesh sieve, are used as one of the ingredients in "auxiliary product D";

7-2. The preparation method of "auxiliary product E - liquid organic soil conditioner product" according to claim 1, which is at least characterized in that: energy grass, or energy grass and cow dung are used as the starting main raw materials, and in the preparation of " When the main product A - hydrophilic decomposable fiber product" and "by-product C - lignin/resin mixture product", the pressing liquid or/and washing liquid or/and elutriation liquid discharged from the upgraded products A and C ; Then the liquid organic soil conditioner product obtained by blending the "pressed liquid or/and washing liquid or/and elutriation liquid" according to the soil improvement requirements of the crops and plots being applied; the "discharge" The press liquid or/and washing liquid or/and elutriation liquid”, the pH value does not exceed the range of 5.0 to 9.4, and the gram moles of Na + or/and K + or/and Mg 2+ contained therein are equal to those of the The liter volume ratio of water is ≤0.034mol/L, or the total wt% concentration of soluble sodium salts, potassium salts, and magnesium salts contained therein is ≤0.20% (wt%), or the soluble sodium salts, potassium salts contained therein are The difference between the total concentration of salt and magnesium salt and the total concentration of soluble sodium salt, potassium salt and magnesium salt in the water source taken from the production site is ≤0.01% (wt%); the weight ratio of auxiliary product E to main product A is Control within the range of product E/product A ≤ 100/100 ~ 300/100, that is, ≤ 100/100 or ≤ 300/100;

7-3. The preparation method of "auxiliary product F - fermented feed product" according to claim 1, which is at least characterized in that: the "by-product material 1: hot water delignification/resin" described in item ii in claim 2 The brown/black liquor discharged from the process" or/and" or by-product material 2: The fresh juice obtained by squeezing the fresh energy grass will be mixed with the energy grass that has only been broken/crushed, and then fermented to obtain auxiliary products F;

7-4. The preparation method of "auxiliary product G - pellet feed product" according to claim 1, which is at least characterized in that: when dry energy grass without pressing treatment is used as the starting main raw material, the main raw material is screened out. The remaining materials after using the raw materials for Product A are "fine powder passed through a 28 mesh sieve", or/and "energy grass fiber powder with a small soil content and a medium particle size passed through a 28 mesh to no more than 150 mesh sieve", as particles. Ingredients in feed products;

7-5. The preparation method of "auxiliary product H - biomass pellet fuel product" according to claim 1, which is at least characterized in that: the energy grass is crushed and sieved to remove fine fibers that have not passed the 28-mesh sieve. Powder, or a full-component energy grass crushing material, as an ingredient component, or a biomass pellet fuel product with waste plastics added; the "waste plastics" include at least waste agricultural plastic films and waste foam plastics , any one or more combinations of waste chemical fiber fabrics or/and chemical fiber wadding, the "addition" accounting for less than 5% of the total weight of the auxiliary product H, or up to no more than 22%;

7-6. The preparation method of "auxiliary product I - edible fungus planting stick/block product" according to claim 1, which is at least characterized in that: when using energy grass, or energy grass and cow dung as the starting main raw materials, use The remaining materials after sifting out the raw materials for the main product A, namely energy grass powder or fine cow manure sediment that has passed through a 28-mesh sieve, are used as ingredients in the edible fungus planting stick/block product.
The equipment used in the "preparation method" described in claims 4 to 7 is also characterized by the following 8-1 to 8-4 or 8-5:

8-1. Implementing "step one" to "step ten" described in claim 4 involves setting up combined machines I to X:

The combined machine I for implementing the "pretreatment and material preparation" of "Step 1" described in claim 4 at least includes:

Set up any or multiple combinations of crushing machinery 1, sawing/grinding/cutting/hammer crusher 2, air separation machinery 3, and mechanical screen 4 to crush the energy straw bundles and saw/grind/cut them. /hammer, and then through air selection and screening, screen out the classified or mixed particles of any mesh size from 3 mesh to 28 mesh in the energy grass crushed material. The elongated fiber bundles with a diameter of 100 mm or more; or a puffing machine 5 is installed after the mechanical screen 4 to realize the mechanical puffing treatment of the elongated fiber bundle energy grass crumbs that have been removed, purified and screened; thus Mechanical settings of 1, 2, 3, 4, and 5 to achieve right alignment Implementation of the "pre-treatment preparation" in step 1 of requirement 4 - obtaining backup energy grass crumbs that can be processed in step 2; backup energy grass crumbs

The combined machine II for implementing the "first batching" of "step two" in claim 4 at least includes:

Set up a batching warehouse 6 for placing "backup energy grass crumbs", a liquid tank 7 for holding the extruded water obtained from the "second solid-liquid separation" described in the subsequent step seven, or a tank for storing "surfactant" The silo 8 is equipped with a weighing scale 9 and a mixing agitator 10 after the "first batching"; thus, the mechanical settings of 6, 7, 8, 9, and 10 realize the second step in claim 4. The realization of “first batching”;

The combined machine III for implementing the "heating dissolution" of "step three" in claim 4 at least includes:

Set up a tank 11 for stirring, mixing, heating and insulation; with this mechanical arrangement of 11, the "natural dry material of 'standby energy grass crushed material' material: 100 parts by weight" and " The "extruded water obtained from the second solid-liquid separation" described in the subsequent step seven: "2x parts by weight", or the surface of 0.1 to 0.3% of the "extruded water" 2x parts by weight Active agent'", place these materials in a tank 11 that can be stirred, mixed, heated and insulated, and perform the operations of evenly stirring and heating the materials to above 70°C, and retaining them;

A combined machine IV is used to implement the "first solid-liquid separation" of "step four" in claim 4, which at least includes:

Set up a conveying machine 12, a screw or roller squeezer 13, a solid-liquid separator 14, and a storage tank 15 to store the "pressed/extruded brown/black liquor" obtained from the "first solid-liquid separation"; thus The mechanical settings of 12, 13, 14, and 15 realize the introduction of the material after the heating and heat preservation operations described in step 4 of claim 4 into a screw or roller extruder, and crush the fiber bundles of the material. kneading treatment, and then introduce the material into the solid-liquid separator for solid/liquid separation", "or directly introduce the material after the above heating and heat preservation operations into the solid-liquid separator for solid/liquid separation";

The combined machine V for implementing the "second batching" of "step five" in claim 4 at least includes:

Set up a storage bin 16 for placing the "moist material of the hydrophilic decomposable fiber intermediate product A to be processed", a liquid tank 17 containing the extruded water obtained from the "third solid-liquid separation" described in the subsequent step ten, or Set up a silo 18 for storing "whisker additives", set up a weighing scale 19, and set up a mixing agitator 20 for "second batching"; thus the mechanical settings of 16, 17, 18, 19, 20 are implemented The mechanized operation of "step five" in claim 4;

The combined machine VI for "grinding and eliminating latent" in "Step 6" described in claim 4 at least includes:

A high-consistency refiner 21 is provided. A storage bin 22 for materials to be processed is provided in front of the feed port of the high-consistency refiner 21. A conveyor mechanism or conveyor is provided between the storage bin 22 and the high-consistency refiner 21. Machinery 23; after the discharge port of the high-consistency refiner 21, a submersible tank 24 with a heat preservation or heating function is provided, between the discharge port of the high-consistency refiner 21 and the feed port of the submersible tank 24. time, a conveying mechanism or conveying machine 25 is provided; thus the mechanical arrangements of 21, 22, 23, 24, and 25 realize the mechanized operation of "step six" in claim 4;

The combined machine VII for implementing the "second solid-liquid separation" of "step seven" in claim 4 at least includes:

Conveying machinery 26, a screw or roller squeezer 27, a solid-liquid separator 28, and a storage tank 19 for storing the "extruded water obtained from the 'second solid-liquid separation'" described in step seven of claim 3 are provided. ;Thus, the mechanical settings of 26, 27, and 28 realize the mechanized operation of "step seven" in claim 4;

The combined machine VIII for implementing the "third batching" of "Step 8" described in claim 4 at least includes:

A storage bin 29 is provided for storing the "tidal material of the hydrophilic decomposable fiber intermediate product B to be processed" described in step seven of claim 4, a storage tank 30 for metering and storing new water and circulating purified water, and a material for storing whisker additives. Chamber 31, weighing scale 32, stirring and mixing tank 33; thus the mechanical arrangement of 29, 30, 31, 32, 33 realizes the mechanized operation of "step eight" in claim 4;

The combined machine IX for implementing the "stirring and washing" of "step nine" in claim 4 at least includes:

After the aforementioned "stirring and mixing tank 33", a conveying mechanism or conveying machine 34, a screw or roller squeezer 35, and a temporary material storage tank 36 are provided; thus, the mechanical arrangement of 34, 35, and 36 realizes the claim 4 The purpose of the process described in step 9: Introduce the "'third batching'" into the screw or roller squeezer, perform a mechanical kneading treatment on the fiber bundles of the material, and then introduce the material into the final drying process. Temporary material storage tank; or directly introduce the above 'third batching' into the mixer for stirring, so that the new water and the old water originally contained in the moisture solid phase fiber of the hydrophilic decomposable fiber intermediate product B can be fully mixed. Then the material is introduced into the temporary storage tank for the material to be finally squeezed dry";

A combined machine X is used to implement the "third solid-liquid separation or final modification" of "step ten" in claim 4, which at least includes:

Set up a conveying mechanism or conveying machinery 37, a solid-liquid separator 38, a trough 39 for storing iron/manganese ion masking additives, and a trough 40 for storing anti-mildew additives; thus the mechanical settings of 37, 38, 39, and 40 , to achieve the purpose of the process described in step ten in claim 3: to obtain the "extruded water obtained from the 'third solid-liquid separation'" as described in step five in claim 4, and the final product - including A- 1 or/and A-2 hydrophilic and decomposable fiber A as the main product; or and then make final modifications to reduce product discoloration and mildew;

8-2. Equipment used to implement the "joint production method" described in claim 5, involving the installation of combined machinery XI to XIII:

The combined machinery XI used to implement the "co-production of A and C-1" described in 5-1 and 5-2 of claim 5 at least includes:

In view of the specific production method described in 5-1 of claim 5, an operating machine 41 is provided for removing the roots and leaves of the fresh energy grass, and a cleaning machine 41 is provided for washing, dehydrating and drying the fresh energy grass. The machine 42 is equipped with a press 43 for squeezing and extracting juice from "fresh energy grass washed with water", a storage tank 44 for storing the fresh juice of the squeezed energy grass, or a press 43 for heating the fresh juice to boiling or evaporation to thicken it. The distillation kettle 45 is equipped with cooling and canning machinery 46; through the 41, 42, 43, 44, 45, 46 set up here, it is possible to extract juice from fresh energy grass through root removal, leaf removal, water washing, dehydration, and squeezing. Reheating and sterilizing, evaporation and concentration, cooling, filling, or mechanical processing until heating and evaporation to dryness, to obtain edible food that can be in the form of a tan colloid in the form of pasta, or in the form of coffee-colored powder or granules, or in the form of rosin-like solid blocks. or medical grade lignin/resin mixture by-product C-1;

And for the specific production method described in 5-2 of claim 5, an operating machine 47 is provided for removing roots and leaves of the dry energy grass, or a combined machine 48 is provided for crushing and screening the dry energy grass material. , set up a cleaning machine 49 for washing and dehydrating the dried energy grass, a combined machine 50 that can add water, heat it to boiling, and then extract the juice, and a storage tank 51 for storing the squeezed energy grass juice, The "energy grass juice" is also the by-product material 2 described in item ii of Example 2 - "the juice obtained by washing the dried energy grass with water and then boiling and pressing it"; or another set of "juice" "Energy Grass Juice" is used to make a distillation kettle 52 that is heated to boiling or evaporated to concentrate, and a cooling and canning machine 53 is set up; through the 47, 48, 49, 50, 51, 52, 53 set up here, the dry energy grass is realized. Root removal, leaf removal, crushing, sieving, washing, dehydration, hot water soaking, pressing to extract juice, then heat sterilization, evaporation and concentration, cooling, filling, or mechanical processing until it is heated and evaporated to dryness to obtain a form that can be presented. Edible or medical grade lignin/resin mixture by-product C-1 in the form of paste-like brown colloid, or coffee-colored powder or granules, or rosin-like solid block;

The combined machinery XII used to implement the "co-production of A and C-2" described in 5-3 to 5-5 of claim 5, at least includes:

In view of the specific production method described in 5-3 of claim 5, an operating machine 54 is provided for removing roots and leaves of fresh energy grass, a press 55 is provided for pressing and extracting juice from fresh energy grass, and a press energy storage device is provided. A storage tank 56 for the fresh juice is provided, or a distillation kettle 57 for heating the fresh juice to boiling or evaporation and concentration is provided, and a cooling and canning machine 58 is provided; through the 54, 55, 56, 57, 58 set up, Realize the mechanical treatment from fresh energy grass, through root removal, leaf removal, squeezing and juice extraction, then heat sterilization, evaporation and concentration, cooling, filling, or until heat and evaporation to dryness, to obtain a tan colloid that can be in the form of a paste. , or feed or industrial grade lignin/resin mixture product C-2 in the form of brown powder or granules, or rosin-like solid blocks;

For the specific preparation method described in 5-4 of claim 5, an operating machine 59 for removing roots and blades of dry energy grass is provided, or a combined machine 60 for crushing and screening the dry energy grass material is provided. A combined machine 61 that can add water, heat it to boiling, and then extract juice is provided, and a storage tank 62 is provided that stores the squeezed energy grass juice. The "energy grass juice" is also described in item ii of claim 2. By-product material 1 - brown/black liquor discharged from the hot water delignification/resin process; or a distillation kettle 63 for heating the "energy grass juice" to boiling or evaporation and concentration, and cooling and canning machinery are installed. 64; Through the settings 59, 60, 61, 62, 63, and 64, it is possible to extract juice from dry energy grass by removing roots, removing leaves, crushing, sifting, soaking in hot water, pressing, and then heating, sterilizing, and evaporating Concentrate, cool, fill, or mechanically process until it is heated and evaporated to dryness to obtain edible or medical grade lignin that can be in the form of a paste-like brown colloid, or a coffee-colored powder or granule, or a rosin-like solid block/ Resin mixture by-product C-2;

For the specific preparation method described in 5-5 in claim 5, a storage tank 65 is provided for storing the dewatered water after "cleaning" the energy grass in the combined machine XI, and a storage tank 65 is provided. A combined machine 66 for washing and screening cow dung with outflow water, a combined machine 67 for adding water, heating to boiling, and then squeezing the juice, and a storage tank 68 for storing the squeezed energy grass juice, as described in " The "energy grass juice" is also the by-product material 1 described in claim 2 item ii - brown/black liquor discharged from the hot water delignification/resin process; or it is further configured to heat the "energy grass juice" to boiling Or the distillation kettle 69 for evaporation and concentration is equipped with cooling and canning machinery 70; through the 65, 66, 67, 68, 69, 70 set up here, the cow dung can be washed, screened, soaked in hot water, and squeezed to extract juice. , then heat and sterilize, evaporate and concentrate, cool, fill, or mechanically process until it is heated and evaporated to dryness to obtain a paste-like brown colloid, or a coffee-colored powder or granule, or a rosin-like solid block. Edible or medical grade lignin/resin mixture by-product C-2;

The combined machinery XIII used to implement the details of "can be moved later" and "can be guided subsequently" described in 5-6 of claim 5, at least includes:

Set up a classification collection bin 71 to collect the "pressed dregs" of energy grass or cow dung exported by the combined machines XI and A combined machine 72 for stirring and heating floss-like materials; a mechanical sieve 73 is set up to screen the elongated fiber bundles with particle size classification or mixing ranging from 3 mesh to no more than 28 mesh sieve holes in the foamed material; and is set up to collect A collection bin 74 for "elongated fiber bundles with particle sizes ranging from 3 mesh to no more than 28 mesh sieves or mixed"; a "storage bin 16" that guides the materials in the collection bin 74 to the aforementioned "combined machine V" is provided "Conveyor machinery 75, so that the material is classified into the "moist material from which the water solute in the fiber has been initially removed and the hydrophilic decomposed fiber intermediate product A to be treated" described in step 4 of claim 4, and can be followed by the right Through the operations of the fifth to tenth steps in claim 4, the hydrophilic decomposable fiber product A-1 or A-2 can finally be obtained; a collection tank 76 is provided to collect the "cow dung" described in 5-5 in claim 5. The water containing cow dung produced by "washing and sifting with water" is the "by-product material 3: washing/washing liquid produced by washing/washing cow dung" described in claim 2 item ii ”, which can subsequently be directed to be one of the ingredients of the “auxiliary product E—liquid organic soil conditioner” described in claim 1;

8-3. The equipment used to implement the "preparation method" of "B" described in claim 6 involves setting up sub-assembly machines XIV to XVII, including:

Set up the "material preparation" sub-assembly device XIV of 6-1 in claim 6, which further includes: a mechanical screen 77, or a crushing machine 78 and a winnowing machine 79;

Set up and implement the "ingredients" sub-assembly device ⅩⅤ of 6-2 in claim 6, which further includes: a weighing scale 80, respectively storing "wood" and "plastic" in the composition of the "wood-plastic composite recycled material coarse particles" And the storage bin 81 of the softener, and the mixing tank 82 after metering and batching;

Set up and implement the "granulation" sub-combination device XVI of 6-3 in claim 6, which further includes: a conveying machine 83 and a coarse granulator 84;

Set up and implement the "homogenizing mixing" and "weighing packaging" sub-assembly device Ⅹ Ⅶ of 6-4 to 6-5 in claim 6, wherein Also includes: homogenizing mixer 85, weighing and packaging machinery 86;

8-4. The equipment used to implement the "manufacturing method" of the "auxiliary product" described in claim 7 involves setting up sub-assembly machines XVIII to IIIII, including:

Set up and implement the sub-assembly device XVIII used in the preparation method of 7-1 "auxiliary product D - solid organic soil conditioner" in claim 7, which is characterized in that: it includes a set of assembly devices 87 for preparing solid organic soil conditioner; to realize When "energy grass, or energy grass and cow dung" is used as the starting main raw material, the remaining material after extracting the raw materials for making the main product A is used, that is, energy grass powder or fine cow dung that has passed through a 28-mesh sieve. Sediment, used as an ingredient in "auxiliary product D" for process purposes;

Set up and implement the sub-assembly device XIX used in the preparation method of 7-2 "auxiliary product E - liquid organic soil conditioner" in claim 7, which is characterized in that: it includes a set of assembly devices 88 for preparing liquid organic soil conditioner products; To achieve the technological purpose of using "by-product material 1" or/and "by-product material 3" described in item ii of claim 2 as ingredients in "auxiliary product E";

Set up and implement the sub-assembly device Ⅱ The purpose of the process of adding "by-product material 1" or/and "or by-product material 2" mentioned in item ii to energy grass that has only been broken/pulverized and then fermenting it to obtain auxiliary product F;

Set up and implement the sub-assembly device Ⅱ Ⅰ used in the preparation method of 7-4 "auxiliary product G - pellet feed" in claim 7, which is characterized in that: it includes a set of assembly devices 90 for preparing pellet feed products; to achieve the purpose of screening out the pellet feed products The remaining materials after using the raw materials for the main product A are "fine powder passed through a 28 mesh sieve", or/and "energy grass fiber powder with a small soil content and a medium particle size passed through a 28 to less than 150 mesh sieve", as The technological purpose of the ingredients in pellet feed products;

Set up the sub-assembly device II II used to implement the 7-5 "auxiliary product H - biomass pellet fuel" preparation method in claim 7, which is characterized in that: it includes a set of assembly devices 91 for preparing biomass pellet fuel products; to realize the "The energy grass is crushed and sieved to remove the fine powder that has not passed the 28-mesh sieve, or the full-component energy grass crushing material is used as the ingredient, or waste plastic is added." The technological purpose of the material pellet fuel product;

Set up and implement the sub-assembly device II III used in the preparation method of 7-6 "auxiliary product I - edible fungus planting stick/block" in claim 7, which is characterized in that: it includes a set of assembly devices 92 for preparing edible fungus planting stick/block products ; In order to realize "using energy grass, or energy grass and cow dung as the starting main raw materials, the remaining material after sifting out the raw materials for the main product A, that is, the powder or fine energy grass that has passed through a 28-mesh sieve. The purpose of the process is to use cow dung sediment as an ingredient in edible fungus planting sticks/block products;

8-5. Alternatively, each unit of machinery from 1 to 88 as described in 8-1 to 8-4 above can be arranged neatly into a standard container.
The uses of the "product" or/and "preparation method" or/and "equipment" described in claims 1 to 8 at least include any one or a combination of more of the following:

9-1. "Main product A - hydrophilic decomposable fiber" described in claims 1 and 2, its use can be used at least to prepare rice seedling paper, corrugated paper, cardboard, or/and include egg trays, convenient dinner plates/bowls It can be used as an alternative material to partially or completely replace waste paper recycled pulp in paper molded products including paper seedling pots/bowls; it can also be used as a new starting material for further processing, such as making bleached pulp; or As a raw material for preparing cellulose ether;

9-2. The "by-product B - wood-plastic composite recycled coarse particles" described in claims 1 and 3 can be used at least as wood plastic particles to be modified or/and refined for hot extrusion of wood-plastic products. raw material, or directly used as a new formulation raw material for hot extrusion wood plastic products, or as a granular fuel for heating;

9-3. The "by-product C-1 - edible or medical grade lignin/resin mixture" described in claim 1 can be used at least as a raw material for preparing beverages or/and traditional Chinese medicine preparations;

9-4. The "by-product C-2 - feed or industrial grade lignin/resin mixture" described in claim 1 can be used at least as a feed raw material, or/and as a water-reducing agent for concrete and rubber. /Any kind of softener in plastics;

9-5. The "products", "preparation methods" and "equipment" described in claims 1 to 8 can be used at least for the "raw materials" described in item i of claim 2, including Giant Juncao, etc. Processing; or be expanded to the processing of bamboo, sugar cane bark, palm oil fruit bunch branches;

9-6. The "products", "production methods" and "equipment" described in claims 1 to 8 can all become independent commodities.
The business operation model of the “product” or/and “process” described in any one or more of claims 1 to 9 at least includes any one or a combination of the following:

10-1. One enterprise can independently implement the commercial operation of "products" or/and "manufacturing methods";

10-2. Multiple companies can divide "product" varieties, or/and segment "manufacturing" processes to collaboratively implement commercial operations;

10-3. The business model of self-operated or outsourced manufacturing can be used to implement the commercial operation of "products" or/and "manufacturing methods";

10-4. The described commercial operations, which use agricultural products including solid/liquid organic soil conditioners, and barter with farmers or farming operators for energy grass including straw from grain, cotton and oil fields.