Patent classifications
C05F17/50
Organic slow-acting fertilizer using plantaginis semen husk and manufacturing method therefor
The present invention provides organic slow-acting fertilizer using psyllium seed husk and a method for producing the same. Macroelements or secondary elements selected from 12 essential nutrient elements (N, P, K, Ca, Mg, S, Fe, Mn, Cu, B, Mo, and Zn) for edible plants are extracted from each of oil cake (collectively referring to residue remaining after extraction of vegetable oil, and including soybean oil cake, palm oil cake, etc.), blood meal (livestock blood), dead fish or bonefish-containing by-products, bone meal, Dead Sea mineral, egg shell, seashell, oystershell, natural gypsum, dolomite, phyllite, and natural salt, by a predetermined extraction process, and are impregnated in larger amounts into a porous material such as zeolite, and organic fertilizers are produced in the form of psyllium seed husk-bound grains for more rapid and effective impregnation so that suitable proportions of element fertilizers can be supplied to each type of plant.
Bio-methanol production
Methods and systems for producing bio-methanol can include anaerobic digestion of a biomass feedstock to produce biogas including methane and carbon dioxide, partial oxidation of the biogas with oxygen from water electrolysis to produce syngas, synthesizing bio-methanol from the syngas and hydrogen from the water electrolysis, storing the bio-methanol, intermittently using battery based electricity to power the electrolysis during peak electricity demand, and intermittently using renewable electricity from another source during off-peak demand. Electricity can also optionally be obtained by periodically combusting a portion of the bio-methanol. The techniques provide a route for the production of bio-methanol without the engagement of fossil fuels as feedstocks and mitigating fossil fuel derived greenhouse gas emissions from processing and utilization of transportation fuels and commercial or industrial alcohols.
Bio-methanol production
Methods and systems for producing bio-methanol can include anaerobic digestion of a biomass feedstock to produce biogas including methane and carbon dioxide, partial oxidation of the biogas with oxygen from water electrolysis to produce syngas, synthesizing bio-methanol from the syngas and hydrogen from the water electrolysis, storing the bio-methanol, intermittently using battery based electricity to power the electrolysis during peak electricity demand, and intermittently using renewable electricity from another source during off-peak demand. Electricity can also optionally be obtained by periodically combusting a portion of the bio-methanol. The techniques provide a route for the production of bio-methanol without the engagement of fossil fuels as feedstocks and mitigating fossil fuel derived greenhouse gas emissions from processing and utilization of transportation fuels and commercial or industrial alcohols.
BIOREFINERY METHOD AND SYSTEM FOR ISOLATED ENVIRONMENTS
A Biorefinery System (BIOSYS) that effectively treats all human activity-derived waste (black water, grey water, and food waste streams) using biological systems and that produces as process by-products: recovered potable water, liberated free oxygen, edible protein cake (with and without lipids), soil amendments, and machinery lube oils. Additionally, the system captures and chemically binds carbon dioxide into microbial cells and associated by-products, thus producing recovered usable returned cabin air.
LIGHTWEIGHT APPLIANCE WITH EXOSKELETAL SUPPORT RESPECTIVE KIT-OF-PARTS AND METHOD FOR PRODUCTION OF BIOGAS AND LIQUID FERTILIZER
An assemblage appliance and method of recycling organic waste into biogas and liquid fertilizer, implementing essentially anaerobic digestion processes, is described. The assemblage appliance includes: a pliant structured exoskeletal envelope, pliable collapsible anaerobic digester and gas tank. A compact kit-of-parts for assembling the aforementioned appliance and respective method using the aforementioned appliance for recycling organic waste into biogas and liquid fertilizer are described.
Organic flocculant and fertilizer
Provided herein is technology relating to organic fertilizers and particularly, but not exclusively, to organic and/or biodegradable flocculants, methods of preparing organic fertilizers using an organic and/or biodegradable flocculant, and systems for treating water using an organic and/or biodegradable flocculant to prepare an organic fertilizer.
Agroindustrial process with minimal environmental impact
An agro-industrial process with minimal environmental impact, of the type having a step of cultivating vegetable and/or mushroom products, includes a step of harvesting the products, at least one step of thermo-mechanical treatment of the products in order to obtain intermediate products, and a step of packaging of a final stage of the intermediate products. The thermo-mechanical treatment step provides for a mechanical process of removing the unnecessary parts from the products so as to define waste. The waste, constituted exclusively by vegetable substances, is separated from the intermediate products, intended for the subsequent treatment and packaging steps, and sent into a biogas production unit. The digestate, constituted by the waste of the biogas production unit, is used as a fertilizer on the respective cultivation soil in a new step of cultivation of vegetable products.
Agroindustrial process with minimal environmental impact
An agro-industrial process with minimal environmental impact, of the type having a step of cultivating vegetable and/or mushroom products, includes a step of harvesting the products, at least one step of thermo-mechanical treatment of the products in order to obtain intermediate products, and a step of packaging of a final stage of the intermediate products. The thermo-mechanical treatment step provides for a mechanical process of removing the unnecessary parts from the products so as to define waste. The waste, constituted exclusively by vegetable substances, is separated from the intermediate products, intended for the subsequent treatment and packaging steps, and sent into a biogas production unit. The digestate, constituted by the waste of the biogas production unit, is used as a fertilizer on the respective cultivation soil in a new step of cultivation of vegetable products.
AQUEOUS AND SOLID AMMONIUM SULFATE FERTILIZERS AND METHODS OF PRODUCING
Aqueous and solid ammonium sulfate fertilizers derived from an organic feedstock and a mineral sulfate compound. The aqueous fertilizers have at least 3.5% nitrogen and at least 4% sulfur, and the solid fertilizers have about 21% nitrogen and about 24% sulfur. Methods for producing the fertilizers include preparing an organic feedstock by causing organic waste to undergo anaerobic digestion, removing solids from the organic feedstock to produce an organic liquid effluent, performing a distillation process on the organic liquid effluent to strip and concentrate a vapor that contains ammonia, carbon dioxide, and water and cool the vapor to produce a condensed solution containing ammonium bicarbonate and/or ammonium carbonate, and contacting the condensed solution with the mineral sulfate compound to cause a reaction therebetween and produce an aqueous ammonium sulfate product. An evaporation process can be performed on the aqueous ammonium sulfate product to produce a dry, solid ammonium sulfate product.
DEVICE FOR PRODUCING BIOGAS WITH HIGH METHANE CONTENT BY UTILIZING LIVESTOCK AND POULTRY FECES
The invention discloses a device for producing biogas with high methane content by utilizing livestock and poultry feces, wherein the interior of a tank body of a biogas fermentation tank is divided by a baffle, so as to form a main reaction chamber and an auxiliary reaction chamber which are communicated in upper portions, so that a reactant flows into the auxiliary reaction chamber only after entering the main reaction chamber via a relatively low feeding hole and then reaching a high position of a liquid level, and extension of fermentation time is realized, meanwhile, scales formed at the top of fermentation broth flow into the auxiliary reaction chamber along with liquid, so that the interior of the main reaction chamber keeps a liquid state all the time, and sealing and reduction of quantity of anaerobic bacteria are avoided.