子分类：
| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 121 | 게르마늄 함유 비료 및 이를 이용한 식물 재배 방법 | KR1020100125077 | 2010-12-08 | KR1020120063903A | 2012-06-18 | 한경철; 정금수; 한선웅 |
| PURPOSE: A fertilizer which contains germanium and a plant cultivation method using thereof are provided to increase content amount of germanium in order to facilitate absorbing germanium into plants. CONSTITUTION: A manufacturing method of fertilizer which contains germanium comprises the following steps: stirring 50-60 wt% of coal ash, 20-40 wt% of coal briquette ash, and 10-20 wt% of biotite in boiling water for 24 hours and filtering the mixture in order to manufacture a solution which contains germanium; cultivating pseudomonas putida ATCC 33015 at 27-30 deg. Celsius for 24 hours and adding the cultivated bacteria in bean-curd liquid or soymilk at 27-30 deg. Celsius for 24 hours in order to cultivate microorganism culture; mixing 10 parts by weight of the microorganism culture with 100.0 parts by weight of germanium solution in order to manufacture microbe which contains germanium; mixing the germanium solution and microbe material in a volume ratio of 3:1 and spraying the mixed material on dropwort plant; and fermenting the mixed material at 27-30 deg. Celsius for 10 weeks to 6 months. | ||||||
| 122 | 물 함유 물질의 건조 장치 및 방법 | KR1020097027239 | 2008-06-03 | KR1020100028578A | 2010-03-12 | 독테르반레이우엔,기즈스버트 |
| Method and device for drying a water-containing substance using an air stream by: · heating the air stream in a first heat exchanger (1) by direct contact between the air stream and a first portion of the water-containing substance; · separating the heated air stream into a first and a second air stream; · heating the second air stream in a heating unit (3); · drying a second portion of the water-containing substance in a drying unit (5) by direct contact between the heated second air stream and the second portion of the water-containing substance; · cooling the second air stream to the temperature level of the first cooling liquid in a second heat exchanger (201a) using a first cooling liquid; · mixing the cooled second air stream and the first air stream in a mixing unit; · cooling the mixed air stream by means of a second cooling liquid in a third heat exchanger (201b). | ||||||
| 123 | 수분함유물질의 건조방법 및 시스템 | KR1020097011305 | 2007-11-02 | KR1020090097859A | 2009-09-16 | 닥테르반리우벤,헤이스베르 |
| A method and system for drying a water containing substance, such as manure, into a single dry product, wherein an airflow is conditioned, in order for the airflow to be able to take up moisture, and wherein a substance / airflow interface is provided, in order to allow the air to take up moisture from the substance at the interface to thereby dry the substance, wherein the method comprises the steps of heating the airflow, separating the substance in a relatively solid fraction and a liquid, using the relatively solid fraction to create a first, static substance / airflow interface, using the liquid fraction to create a second, dynamic substance / airflow interface, guiding the airflow to the first substance / airflow interface to dry the relatively solid fraction of the water containing substance, and thereafter guiding the airflow to the second substance / airflow interface to pre-dry the liquid fraction of the water containing substance, mixing the pre-dried liquid fraction with water containing substance. | ||||||
| 124 | 슬러리 분리 및 바이오가스 생산 기술 | KR1020037002640 | 2001-08-22 | KR1020030045040A | 2003-06-09 | 본데토르벤에이.; 페더슨라스죄르겐 |
| 본 발명은 동물성 퇴비, 에너지 작물 및 유사 유기 물질의 혐기성 소화에 관한 것이다. 본 방법은 소화된 바이오매스에 포함된 영양분을 상업적 품질의 비료로 정제할 수 있다. 본 발명은, 동물 기원의 유기 폐기물질을 처리하고 동시에 비료의 생산을 용이하게 하기 위한 대체적 수단을 제공하고자 하는 목적으로, 동물 사체 또는 수육 및 뼈가루 등을 포함하는 이들의 일부분을 처리하기 위한 방법을 또한 제공한다. 따라서, BSE 프리온 또는 다른 어떤 프리온의 동물 또는 인간으로의 확산 위험은 방출되지 않는다면 실질적으로 줄어든다. 본 발명에 따른 바이오가스 및 슬러리 분리 시스템은 축산 기술과 함께 축산의 내부적 및 외부적 실시(performances)가 최적화된 전체적 개념 내로 통합되는 것이 바람직하다. 내부적 실시는 동물 사육장의 운영에 관련된 질적인 측면과 관련이 있고, 산업 위생, 동물 복지, 가스 및 먼지 방출 및 식품 안정성을 포함한다. 외부 실시는 주로 에너지 생산 및 환경으로의 영양분 및 온실 가스의 방출 및 고 품질 식품 산물의 판매와 관련이 있다. | ||||||
| 125 | Process For Manufacturing Liquid And Solid Organic Fertilizer From Animal Manure | US16005002 | 2018-06-11 | US20190010094A1 | 2019-01-10 | Sushil K. Bhalla; Gregory J. Dicosola; Devon K. Hooper; Sarabjit S. Randhava; Michael A. Laughlin |
| Processes for manufacturing organic fertilizer products, such as liquid and solid organic fertilizer, from animal manure are disclosed, together with the fertilizer products produced therefrom. | ||||||
| 126 | MICROBIAL SOIL ENHANCEMENTS | US15499137 | 2017-04-27 | US20180311712A1 | 2018-11-01 | Khanh Le |
| A method for forming soil enhancement includes forming microbes in a concentrated form of at least 1×107 cfu/ml (colony-forming units per milliliter); and dry forming the microbes onto humic acid. | ||||||
| 127 | DEVICE FOR TREATING A SLURRY BY SEPARATING SOLIDS FROM LIQUIDS | US15801248 | 2017-11-01 | US20180117505A1 | 2018-05-03 | Gener Romeu Guardia |
| A device includes a compartment for separating the solids and liquids. The compartment includes a base that is concavely curved according to a cylindrical portion having a transverse axis and is formed of a sieve, an idler roller mounted transversely on an arm, a drive which actuates the arm, and resilient means for adjusting the pressure exerted by the rollers. Both the contact interface between the sieve and the roller and the rotational interface between the roller and the arm are made of a non-metal material on at least one of the two contacting surfaces that form each of the interfaces, such that, there is no metal-on-metal contact between surfaces moving relative to one another at the interfaces. | ||||||
| 128 | Separation of clean water from effluent streams | US15789996 | 2017-10-21 | US09956563B1 | 2018-05-01 | Aicardo Roa-Espinosa; Samuel William Roa-Lauby; Kim Huong Pham; Joaquin Camilo Perez-Mahecha |
| A process for separating clean water which has an impurities content of less than 100 ppm from waste materials such as farm manure is disclosed. In a first step, a plate separator splits the waste material stream into a first effluent fraction and a first solids fraction. The first solids fraction then undergoes two stages of pressing to increase the solids contents to about 30 to 40 percent which makes it suitable for granulation or pelletizing. The first effluent fraction is treated in successive stages with various chemical agents resulting in the removal of most of the solids and inorganic impurities from the effluent to achieve drinkable water purity. | ||||||
| 129 | Process for manufacturing liquid and solid organic fertilizer from animal waste | US14623602 | 2015-02-17 | US09688584B2 | 2017-06-27 | Sushil K. Bhalla; Gregory J. Dicosola; Devon K. Hooper; Sarabjit S. Randhava; Michael A. Laughlin |
| Processes for manufacturing organic fertilizer products, such as liquid and solid organic fertilizer, from animal manure are disclosed, together with the fertilizer products produced therefrom. | ||||||
| 130 | Method for treating animal waste | US13591995 | 2012-08-22 | US09643868B2 | 2017-05-09 | William Blaine |
| Methods and apparatus for the treatment of animal waste are disclosed, together with a treated animal waste and fertilizer and growth media products derived therefrom. | ||||||
| 131 | Method for treating and/or pretreating liquid manure or biogas plant reject for the elimination of harmful substances, particularly nitrogen, phosphorus, and odor molecules | US12937604 | 2009-04-24 | US09527759B2 | 2016-12-27 | Anni Alitalo; Erkki Aura; Risto Seppälä |
| The invention relates to a method and an apparatus for treating and/or pre-treating liquid manure or biogas plant reject for eliminating harmful substances, particularly nitrogen, phosphorus, and odor molecules. Process tanks (5), which include inlet means (4) for supplying a process tank (5) with a substance to be treated, outlet means for passing a post-treatment matter out of the tank, and air inlet means (2) for supplying the process tank with air required by a biological process, are used for conducting a biological treatment on the matter to be treated. The process tanks (5) are first provided with a microbe population adapted for treating the matter to be treated. The matter to be treated is supplied gradually into the first process tank and then further into a subsequent process tank, such that the microbe population initially provided in the process tanks displaces in a step-by-step manner the original microbe population present in the matter to be treated. The matter, which is substantially free of the original microbes and has been expelled from the final process tank, is returned into the first process tank for diluting the matter to be treated. Downstream of the process tanks is conducted a nitrogen removal treatment by feeding the matter to be treated from the process tank (5) of a stripping tower (22A), in which the pH of a matter to be treated has been raised by means of a biological treatment to a level sufficient from the standpoint of nitrogen removal. | ||||||
| 132 | Methods and Apparatus Utilizing Vacuum for Breaking Organic Cell Walls | US15028719 | 2014-10-12 | US20160257923A1 | 2016-09-08 | Olaf Lee |
| Moisturized organic material is treated by communicating with a vacuum pump (44) to selectively reduce pressure within a vessel (12) below atmospheric pressure and to a vaporization point, such as at 30 to 17.8 C, for a period of time sufficient to create an internal pressure to rupture cell walls. While being subjected to vacuum below atmospheric pressure, the vessel (12) is rotated to homogenize the moisturized organic material. The organic material can be moisturized by non-potable water including moisture collected by a moisture collector (44b) in the conduit (44a) between the vessel (12) and the vacuum pump (44) and by chilled feed water acting as the seal fluid in the vacuum pump and heated while flowing through a heat exchanger (48) of the moisture collector (44b). Heat can be added by a heater (46) to raise the temperature of low ambient temperature moisturized organic material. | ||||||
| 133 | PROCESS FOR MANUFACTURING LIQUID AND SOLID ORGANIC FERTILIZER FROM ANIMAL WASTE | US14623602 | 2015-02-17 | US20150259259A1 | 2015-09-17 | Sushil K. Bhalla; Gregory J. Dicosola; Devon K. Hooper; Sarabjit S. Randhava; Michael A. Laughlin |
| Processes for manufacturing organic fertilizer products, such as liquid and solid organic fertilizer, from animal manure are disclosed, together with the fertilizer products produced therefrom. | ||||||
| 134 | System and method for drying a water-containing substance | US12663227 | 2008-06-03 | US08365436B2 | 2013-02-05 | Gijsbert Docters van Leeuwen |
| Method and device for drying a water-containing substance using an air stream by: heating the air stream in a first heat exchanger (1) by direct contact between the air stream and a first portion of the water-containing substance; separating the heated air stream into a first and a second air stream; heating the second air stream in a heating unit (3); drying a second portion of the water-containing substance in a drying unit (5) by direct contact between the heated second air stream and the second portion of the water-containing substance; cooling the second air stream to the temperature level of the first cooling liquid in a second heat exchanger (201a) using a first cooling liquid; mixing the cooled second air stream and the first air stream in a mixing unit; cooling the mixed air stream by means of a second cooling liquid in a third heat exchanger (201b). | ||||||
| 135 | LIQUID SEPARATION DEVICE | US13054301 | 2010-09-14 | US20120031856A1 | 2012-02-09 | Alain Courtemanche; Yann Desrochers; Jerome Brisson; Stephane St-Onge |
| A liquid separating device (1) for processing a mixture material (3) containing both solid and liquid materials (3a,3b), in order to separate liquid material (3b) from the solid material (3a), the liquid separating device (1) includes a support frame (5), a series of liquid separation assemblies (7a,7b) and a corresponding guiding assembly (19) between each pair of liquid separation assemblies (7). The liquid separation assemblies (7) are disposed about the support frame (5) in a cascading configuration, and the passage (13) of each liquid separation assembly (7) is narrower in width than the passage of a preceding liquid separation assembly (7) so that each subsequent liquid separation assembly (7b) is enabled to extract more liquid material via an increased wringing pressure resulting from a thickening of the remaining mixture material (3) to be processed and the narrower subsequent passage (13b) through which it is channeled and pressed. | ||||||
| 136 | METHOD FOR TREATING AND/OR PRETREATING LIQUID MANURE OR BIOGAS PLANT REJECT FOR THE ELIMINATION OF HARMFUL SUBSTANCES, PARTICULARLY NITROGEN, PHOSPHORUS, AND ODOR MOLECULES | US12937604 | 2009-04-24 | US20110113840A1 | 2011-05-19 | Anni Alitalo; Erkki Aura; Risto Seppälä |
| The invention relates to a method and an apparatus for treating and/or pre-treating liquid manure or biogas plant reject for eliminating harmful substances, particularly nitrogen, phosphorus, and odor molecules. Process tanks (5), which include inlet means (4) for supplying a process tank (5) with a substance to be treated, outlet means for passing a post-treatment matter out of the tank, and air inlet means (2) for supplying the process tank with air required by a biological process, are used for conducting a biological treatment on the matter to be treated. The process tanks (5) are first provided with a microbe population adapted for treating the matter to be treated. The matter to be treated is supplied gradually into the first process tank and thence further into a subsequent process tank, such that the microbe population initially provided in the process tanks displaces in a step-by-step manner the original microbe population present in the matter to be treated. The matter, which is substantially free of the original microbes and has been expelled from the final process tank, is returned into the first process tank for diluting the matter to be treated. Downstream of the process tanks is conducted a nitrogen removal treatment by feeding the matter to be treated from the process tank (5) of a stripping tower (22A), in which the pH of a matter to be treated has been raised by means of a biological treatment to a level sufficient from the standpoint of nitrogen removal. | ||||||
| 137 | SYSTEM AND METHOD FOR DRYING A WATER-CONTAINING SUBSTANCE | US12663227 | 2008-06-03 | US20110041357A1 | 2011-02-24 | Gijsbert Docters Van Leeuwen |
| Method and device for drying a water-containing substance using an air stream by: heating the air stream in a first heat exchanger (1) by direct contact between the air stream and a first portion of the water-containing substance; separating the heated air stream into a first and a second air stream; heating the second air stream in a heating unit (3); drying a second portion of the water-containing substance in a drying unit (5) by direct contact between the heated second air stream and the second portion of the water-containing substance; cooling the second air stream to the temperature level of the first cooling liquid in a second heat exchanger (201a) using a first cooling liquid; mixing the cooled second air stream and the first air stream in a mixing unit; cooling the mixed air stream by means of a second cooling liquid in a third heat exchanger (201b). | ||||||
| 138 | MANURE SEPARATION FOR DIGESTER METHOD AND APPARATUS | US11868234 | 2007-10-05 | US20090090679A1 | 2009-04-09 | David C. DeWaard |
| A method and apparatus for removing settleable solids and unsettleable solids from a partially closed flush system in a dairy milking operation whereby a first processing tank bottom removes settleable solids contained therein where the net current flow vertically in the process tank is less than the settling rate of the settleable solids contained therein. The process tank batch feeds a plurality of thickening tanks that are each allowed to settle for a period of time before transferring fluid is to a second separator. The method and apparatus uses the solids for feeding a digester. | ||||||
| 139 | Hog manure treatment method | US10522407 | 2002-07-26 | US07410589B2 | 2008-08-12 | Gurunathan Lakshman |
| The invention relates to a method of treating manure such that odor from the manure is significantly reduced or eliminated and producing therefrom recyclable water, value-added biosolids and ammonia. Specifically, the manure is combined with lime at high pH. The material is mixed under negative pressure and the basic conditions cause ammonia to be evolved from the manure which is then drawn off and recovered. A coagulating agent is then added which further promotes floc formation within the manure. Following further mixing, flocs are separated from the liquid portion. A struvite-promoting chemical and a coagulant are then added to the liquid portion which causes further floc formation, and the flocs are again separated from the substantially clear liquid. It is of note that as a result of this process, the solids are highly hydrophobic and dry very quickly. It is of further note that solids isolated from either step can be combined and sold, for example, as fertilizer, as discussed below. The clear liquid can be used, for example, in barn washes or for horticultural watering. | ||||||
| 140 | Method and apparatus for converting spent water-based drilling muds into fertile indigenous top soil | US11396978 | 2006-04-03 | US07272912B2 | 2007-09-25 | Houston E. Hill |
| A method and apparatus for converting spent water-based drilling mud into fertile indigenous top soil at a well site or location. The fertile indigenous top soil is produced by the steps of: admixing, at a well site, effective amounts of spent water-based drilling mud, mature compost, organic fertilizer, and top soil from the well site to provide a mixture containing spent water-based drilling mud, from about 30 to about 150 volume percent mature compost, from about 5 to 20 volume percent organic fertilizer, and from about 5 to 20 volume percent top soil from the well site wherein each of the volume percents is based on the volume of the spent water-based drilling mud present in the mixture; stirring the mixture for a period of time effective to form a substantially homogenous mixture; and drying the substantially homogenous mixture so as to provide fertile indigenous top soil possessing similar microbial and enzyme characteristics as the top soil at the well site. | ||||||
QQ群二维码
意见反馈
意见反馈