264 results about "Waste production" patented technology

The present invention allocates the supply of critical components and manufacturing capacity by optimizing critical material planning decisions and dynamically allocating constrained materials using advanced substitution logic that considers alternate suppliers and supports product life cycle from design through end-of-life. The present invention may utilize unique synchronized allocations and matched sets logic. The synchronized allocations ensure that all materials necessary for production are available in the appropriate time-phased allocation before beginning production to minimize wasted production capacity and materials. The supply system may include various combination of components, including a Supply Planner, a Resource Optimizer, a Constraint Based Master Planner, a Product Change Analyzer, a Comparer, a Resource Requirements Planner, a Finite Resource Planner, a Customer Promiser, and an Interactive Master Scheduler. Another embodiment of the supply system includes a tool that allows users to define products using engineering specifications.

A process for producing organic acid esters using continuous countercurrent reactive distillation using acid catalysts in a structured packing in a single column (10) is described. In the reactive distillation an organic acid ester is formed by chemical reaction and can be purified to its final state within the single column. Organic acid esters are produced at relatively low cost, with less waste production, and in a less complicated manner than prior processes. Organic acid ester have uses as solvents, as intermediate chemicals, and in consumer products.

A process for producing organic acid di- or tri-esters, particularly citric acid tri-esters, with the available acid groups esterified using countercurrent reactive distillation using acid catalysts in a structured packing is described. In the reactive distillation an organic acid di- or tri-ester is formed by chemical reaction and purified to its final state within the single column. Organic acid di- or tri-esters are produced at relatively low cost, with less waste production in by-products of the reaction, and in a less complicated manner than prior processes. Organic acid di- and tri-esters have uses as solvents, as plasticizers and in conversion products.

The present invention provides methods for the synthesis of catalysts and precursors thereof. Methods of the invention may comprise combining a catalyst precursor and at least one ligand to generate a catalytically active species, often under mild conditions and in high yields. In some cases, a wide variety of catalysts may be synthesized from a single catalyst precursor. Methods of the invention may also include the preparation of catalysts which, under reaction conditions known in the art, may have been difficult or impossible to prepare and/or isolate due to, for example, steric crowding at the metal center. The present invention also provides catalyst compositions, and precursors thereof, which may be useful in various chemical reactions including olefin metathesis. In some cases, methods of the invention may reduce the number of synthetic and purification steps required to produce catalysts and/or other reaction products, as well as reducing time, cost, and waste production.

The present invention discloses a preparation method for optical activity active 3-amino butanol and optical activity 3-amino butyric acid. The optical activity active 3-amino butanol preparation method comprises: in a solvent, under effects of a hydroboration reduction agent and a Lewis acid, carrying out a reduction reaction on a compound represented by a formlu 65 to produce a compound represented by a formlu 14. The optical activity active 3-amino butyric acid preparation method comprises: carrying out a hydrolysis reaction on a compound represented by a formlu 64 to produce a compound represented by a formlu 65. According to the present invention, the preparation method has characteristics of cheap and easily-available raw materials, simple operation, short process route, no hazard of raw materials, high yield, little waste production, environment protection, high raw material conversion rate, high product chemical purity and high product optical purity, and the industrialization is easily achieved. The formulas 64, 65 and 14 are defined in the instruction.

The invention discloses a no-waste production method for peeled sweet potato starch. The provided method comprises the following steps: step 1. the sweep potato is peeled and/or the speck is removed; step 2. the sweep potato obtained in the step 1 is squeezed to obtain coarse size and coarse potato residue; and step 3. the coarse size obtained in the step 2 is treated to obtain starch in the coarse size and a first by-product, i.e., sweet potato size; the coarse potato residue obtained in the step 2 is treated to obtain starch in the coarse potato residue and a second by-product, i.e., potato powdered residue; and the coarse size and the washing water obtained during the coarse potato residue treatment are treated to obtain a third by-product containing polysaccharide and protein and water, and the water can be further taken as the washing water for the sweet potato, the starch and the coarse potato residue. The method can utilize all the nutritious substances in the sweet potato and is free from the influence of reduction of the starch content during the storage process of the sweet potato, and the application of the sweet potato size and the concentrated solution of the washing water provides a possibility of prolonging the processing cycle of the sweet potato starch.

A method and system for producing an animal bedding material from recycled waste paper, and including one or more chemical additives. The base material is fiberized, and the chemical additives may include: pesticides, disease immune additives (medicines), ammonia inhibitors, fire retardants, or other additives, depending on the characteristics desired of the final product. At least one of the additives is applied as a liquid.

A thermal reactor for producing usable heat energy by destroying waste including a vessel wherein organic waste upon entering said vessel gasifies as it falls onto a carbon bed and is transformed into a synthesis gas with high heat and kinetic energy that can be harnessed to produce electricity. Inorganic waste upon entering melts as it falls onto the carbon bed and exits via slag ports to form an inert slag. Because there is no oxygen present in the gasification zone, the waste is not combusted and neither furan or dioxin are formed. The waste includes either prepared refuse derived fuel (RDF) or unprepared raw waste or a combination thereof.

The invention relates to a process of extracting abamectin components B1 and B2 step by step by utilizing a crystallization method, comprising the steps of leaching abamectin mycelia by using ethanol (or methanol), subjecting the leachate to preliminary concentration, adding active carbon to decolorize the leachate, converting the solvent into toluene after the decolorization is completed, carrying out cooling crystallization to obtain a mixture of the abamectin components B1 and B2, converting the solvent of the crystallization mother liquor into methanol, carrying out cooling crystallization on the mixture of the abamectin components B1 and B2, obtained in the first crystallization, to obtain crystals i.e. the abamectin component B1, converting the solvent of the mother liquor into toluene and obtaining the components B2 through crystallization. According to the invention, on the premise of not increasing the fermentation cost, the components B1 and B2 are extracted from the mycelia step by step, so that the economic benefit of enterprises is increased, and the resource waste and the waste production are reduced at the same time.

The invention provides a fluorocarbon rubber with easy demoulding and tear resistance and banburying method thereof, comprising the following components: 100 parts of crude fluororubber; 4-6 parts of high activity magnesium oxide; 2-4 parts of calcium hydroxide; 1.5-6 parts of iron oxide red; 0.4-1.0 part of rubber ingredient WS280; 0-1.0 part of rhine 54; 0-1.0 part of brazil carnauba wax; 1.2-2.4 parts of bisphenol AF; 0.4-1.0 part of benzyltriphenylphosphonium chloride; and appropriate calcium silicate or barium sulphate added according to hard requirement. The invention also provides two banuring methods of fluorocarbon rubber with easy demoudling and tear resistance. The product of the invention has good demoulding performance, and the produced trimming after vulcanization can be taken down along with the product, thus reducing clearing time of operators and avoiding waste production caused by reduction of mould temperature. By the improvement of banburying method of fluorocarbon rubber, dispersion performance of fluorocarbon rubber can be improved, thus improving demoulding performance thereof in vulcanization and reducing tear of product, so that scrap rate of product in one specification caused by tear is reduced to 0.15% from 0.36% (reduced by near 60%).

The invention relates to a heating control method of a steel rolling heating furnace applicable to pipeline steel. A four-stage heating mode is adopted. The temperature at the preheating stage is 1100+/-50 DEG C, and the preheating time is more than or equal to 105 min; the temperature at the first heating stage is 1200+/-30 DEG C, and the heating time is more than or equal to 30 min and less than or equal to 60 min; the temperature at the second heating stage is 1220+/-20 DEG C, and the heating time is more than or equal to 35 min and less than or equal to 60 min; the temperature at the uniform heating stage is 1180+/-20 DEG C, and the heating time is more than or equal to 40 min; the temperature of a flue inlet is 750+/-50 DEG C; the heating speed before the temperature of a plate blank is lower than or equal to 600 DEG C is controlled not to be higher than 7 DEG C/min, and the difference between the adjacent lowest temperature and the highest temperature in the length direction of the plate blank is controlled to be lower than or equal to 8 DEG C. By means of the heating control method, the continuity of the plate blank heating process is guaranteed, and plate blank cracks caused by improper heating speed are avoided; the performance stability of the whole plate is effectively guaranteed in the pipeline steel rolling process, and steel wasting production accidents and plate blank black print defects caused by squatting and bending of an intermediate billet are avoided.

A method for treating heavy metal-containing acidic wastewater in nonferrous metal industry adopts a tailings mortar neutralization-vulcanization-coagulation combined process, wherein the major flow of the process comprises the following steps of: neutralizing and absorbing the heavy metal-containing acidic wastewater by using tailings mortar at first, and then putting Na2S in a vulcanization reaction with left heavy metals in the acidic wastewater; next, performing coagulation and sedimentation with FeSO4 as a coagulant and polyacrylamide as a coagulant aid so that H+ in the acidic wastewater is neutralized, thereby removing heavy metals in the wastewater. The method reduces capital investment of an enterprise on wastewater disposal to an utmost extent, and simultaneously reduces the solid waste yield of the enterprise by utilizing the tailings mortar produced in mining and milling of ores; besides, the acidity of the wastewater can be effectively neutralized and the heavy metals can be effective removed.

The invention discloses a method for preparing a calcium carbonate raw material and SO2 by utilizing high-sulfur petroleum coke to decompose phosphogypsum, i.e., the high-sulfur petroleum coke with the carbon mass fraction higher than 80 percent and the sulfur mass fraction higher than 2 percent to 6 percent is used for reducing and decomposing the phosphogypsum to prepare burner gas with the SO2 volume percentage higher than or equal to 15 percent. The burner gas can be directly used as qualified virgin gas for the two-conversion and two-absorption acid-making technology so as to produce the solid product, CaO, with the mass fraction of higher than 50 percent, and can also be directly used as a chemical raw material, for instance, for making cement. No waste is generated in the process, the decomposition rate of the phosphogypsum is higher than or equal to 95 percent, and the desulphurization degree is higher than or equal to 90 percent. By utilizing the technology for decomposing the phosphogypsum, pretreatment is not required and the concentration of SO2 is stable in the burner gas. The content and the thermal value of carbon in the high-sulfur petroleum coke are comparatively high, and the contents of nitrogen and sulfur are higher than that of other fuels, thereby reducing reaction temperature, energy consumption and production cost, simultaneously, environment pollution is not generated and waste is changed into valuable. The utilization of components of the phosphogypsum is maximized during the technical process so as to solve the problem of realizing the harmlessness and sales of the phosphogypsum as 'dangerous waste'.

The invention provides a flocculation adsorption treatment method of waste liquid of a nuclear power plant and a flocculating agent. The flocculation adsorption treatment method includes the steps of adding flocculating agent into the waste liquid of the nuclear power plant, keeping a pH (potential of hydrogen) value within 7-9, performing mixed reaction to obtain colloid flocculation; and subjecting the colloid flocculation to activated carbon adsorption column for adsorption, wherein Fe, Co, Mn and Ag nuclides are absorbed and intercepted by the activated carbon adsorption column. The flocculating agent comprises a component A including NaOH or KOH, a component B which is polyacrylamide, a component C which is sodium polyacrylate or potassium polyacrylate. Coagulation capacity of corrosion product colloids is improved by adding the flocculating agent, and decontamination factor of activated carbon to Fe, Co, Mn, Ag is increased by 5 times. The flocculation adsorption treatment method is stable in eliminating effect, good in repeatability, low in running energy consumption and less in secondary pollution output.

The invention provides a preparation method of 5-methyl-2-mercapto-1,3,4-thiadiazole. The preparation method comprises the following steps of adding ethyl acetate and hydrazine hydrate into a reaction flask having a volume of 500ml, keeping backflow for 2 hours, cooling to obtain an acethydrazide solution, dropwisely adding carbon disulfide into the acethydrazide solution, then feeding NH3 into the acethydrazide solution containing carbon disulfide at a temperature of 40 DEG C, adding a crude thiadiazole product into deionized water, carrying out elution of filter cake several times by distilled water, and carrying out vacuum-drying to obtain a thiadiazole finished product. The preparation method has that advantages that ethanol is not used in synthesis so that solvent-free reactions are realized; under solvent-free conditions, high reactant concentration is conducive to reaction development; solvent-free reactions are easy to operate, saves energy and prevents waste production; and NH3 replaces potassium hydroxide and thus it is avoided that potassium N-acetylhydrazinodithioformate produced in synthesis is dissolved in methanol and dissolution of potassium hydroxide needs a large amount of methanol and thus the part of potassium N-acetylhydrazinodithioformate dissolved in methanol is lost.

The invention provides a community organic matter in-place digestion degradation biogas preparation electrical power generating system. According to the community organic matter in-place digestion degradation biogas preparation electrical power generating system, kitchen waste of each household in a community is smashed into small particle organic waste, and is mixed with toilet wastewater of each household and community green garbage, and high concentration waste water is obtained via concentration; the high concentration waste water is subjected to anaerobic digestion so as to obtain biogas and a digestion liquid; biogas is subjected to desulfuration purifying so as to obtain pure biogas, the biogas is used for generating electric energy via combustion in an internal combustion engine, and electric energy is recycled back to users in the community; the digestion liquid is treated so as to obtain a fertilizer and terminal waste water; and terminal waste water is subjected to simple treatment in septic tanks, and then is discharged into municipal sewage pipe networks. The community organic matter in-place digestion degradation biogas preparation electrical power generating system is capable of realizing pretreatment of waste sources, and in-place anaerobic digestion, so that technological process is short, treatment cost is low; kitchen waste is not stacked or transported, environment pollution is not caused, and transportation cost is reduced; and at the same time, electric energy generated by the community organic matter in-place digestion degradation biogas preparation electrical power generating system can be used, new energy policy subsidies from the government can be obtained, and economic efficiency maximization is realized.