C05F7/00

MANURE PELLETS, AND PROCESS AND EQUIPMENT FOR MAKING THE SAME
20210292254 · 2021-09-23 ·

A pellet made of dried, unfermented livestock manure has N, P and K values in the range of N: 3 to 7 g/kg, as ammoniac and organic nitrogen, P: 2 to 6 g/kg as phosphorus pentoxide and K: 2 to 6 g/kg as potassium oxide (g/kg). The pellet has a hardness exceeding 10 kg and has a shell composed of manure-base lignin. A press roll, including a hollow rotatable drum with a perforated screen, may be used in combination with an endless belt and a scraper to produce the pellet.

MANURE PELLETS, AND PROCESS AND EQUIPMENT FOR MAKING THE SAME
20210292254 · 2021-09-23 ·

A pellet made of dried, unfermented livestock manure has N, P and K values in the range of N: 3 to 7 g/kg, as ammoniac and organic nitrogen, P: 2 to 6 g/kg as phosphorus pentoxide and K: 2 to 6 g/kg as potassium oxide (g/kg). The pellet has a hardness exceeding 10 kg and has a shell composed of manure-base lignin. A press roll, including a hollow rotatable drum with a perforated screen, may be used in combination with an endless belt and a scraper to produce the pellet.

PROCEDURE FOR PROVIDING AND IMPROVING PUMPABILITY OF HIGH TO VERY HIGH BIOSOLIDS CONTAINING DEWATERED SOLID SEWAGE SLUDGE
20210221726 · 2021-07-22 · ·

The invention provides a process for the drying and re-hydration of high solids Biosolids cake to be converted into a pumpable organic liquid fertilizer. This process may be carried out at ambient pressure without aggressive shearing of the mixture of added process water and the high solids Biosolids cake. The drying step removes the bound water, while the re-hydration step includes mixing which breaks down the particulate matter to produce a fairly homogeneous suspension.

PROCEDURE FOR PROVIDING AND IMPROVING PUMPABILITY OF HIGH TO VERY HIGH BIOSOLIDS CONTAINING DEWATERED SOLID SEWAGE SLUDGE
20210221726 · 2021-07-22 · ·

The invention provides a process for the drying and re-hydration of high solids Biosolids cake to be converted into a pumpable organic liquid fertilizer. This process may be carried out at ambient pressure without aggressive shearing of the mixture of added process water and the high solids Biosolids cake. The drying step removes the bound water, while the re-hydration step includes mixing which breaks down the particulate matter to produce a fairly homogeneous suspension.

Method for Preparing N-P Compound Fertilizer from Incinerated Sewage Sludge Ash (ISSA)
20230399269 · 2023-12-14 ·

The present disclosure provides a method for preparing an N-P compound fertilizer from incinerated sewage sludge ash (ISSA), and relates to the technical field of compound fertilizer production. In the present disclosure, the ISSA is used as a main raw material, and a phosphorus-rich supernatant is obtained using high-concentration nitric acid at a low liquid-to-solid ratio. The phosphorus-rich supernatant and aqueous ammonia are mixed to obtain a white precipitate. The white precipitate is dried and pulverized to obtain a high-grade N-P compound fertilizer. The present disclosure realizes the resource utilization of excess sludge in sewage treatment plants.

CDF-DREDGE, DROP-TUBE SEPARATOR AND METHOD OF TREATING WETLAND AREAS
20210198138 · 2021-07-01 ·

A method and system of treating wetland areas includes collecting a slurry that includes sand/large particulates, water, and fines. The sand/large particulates are separated from the water and fines of the slurry. The sand/large particulates is preferably returned to a waterway or beach reclamation project. The water and fines are directed for application to wetland areas.

CDF-DREDGE, DROP-TUBE SEPARATOR AND METHOD OF TREATING WETLAND AREAS
20210198138 · 2021-07-01 ·

A method and system of treating wetland areas includes collecting a slurry that includes sand/large particulates, water, and fines. The sand/large particulates are separated from the water and fines of the slurry. The sand/large particulates is preferably returned to a waterway or beach reclamation project. The water and fines are directed for application to wetland areas.

CDF-DREDGE, DROP-TUBE SEPARATOR AND METHOD OF TREATING WETLAND AREAS
20210198138 · 2021-07-01 ·

A method and system of treating wetland areas includes collecting a slurry that includes sand/large particulates, water, and fines. The sand/large particulates are separated from the water and fines of the slurry. The sand/large particulates is preferably returned to a waterway or beach reclamation project. The water and fines are directed for application to wetland areas.

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.