| 序号 | 专利名 | 申请号 | 申请日 | 公开（公告）号 | 公开（公告）日 | 发明人 |
|---|---|---|---|---|---|---|
| 1 | 用于窑炉干燥的材料的窑炉干燥的方法和设备 | CN201380035516.3 | 2013-06-20 | CN104582493A | 2015-04-29 | 卡伊·西尔伯曼; 德特勒夫·瑞恩伯格; 马提亚斯·本茨 |
| 本发明涉及用于对用于窑炉干燥的材料或窑烘材料进行窑炉干燥的方法，并且涉及尤其用于执行所述方法的设备，所述材料尤其是谷物、伪谷物、油籽或豆科植物，其中所述方法包含：作为处理步骤，提供将要在托盘(20)上处理的窑烘材料，所述托盘具有至少一个开口(21)，形成一层窑烘材料(D)，以及产生气流，尤其是空气气流(L)，其中所述气流，尤其是所述空气气流(L)，穿过该层窑烘材料(D)，是从面向具有至少一个开口(21)的所述托盘(20)中的该层窑烘材料(D)的空间(X)到背对所述托盘(20)中的该层窑烘材料(D)的空间(Y)生成的。 | ||||||
| 2 | ENERGY SAVING BREWING METHOD | US13701604 | 2011-05-31 | US20130095207A1 | 2013-04-18 | Søren Knudsen; Preben Rils; Birgitte Skadhauge; Lene Mølskov Bech; Ole Olsen |
| Barley based beverages are produced in large quantities, employing highly energy consuming methods, for example in the malting and brewhouse facilities for kiln drying and wort boiling operations, respectively. The present invention relates to energy saving methods for preparing barley based beverages, as well as to barley plants useful in such methods. In particular, the invention describes barley plants with combined traits of null-lipoxygenase-1 (null-LOX-1), null-lipoxygenase-2 (null-LOX-2) and null-S-adenosylmethionine:methionine S-methyltransferase in one plant, which is particularly useful for energy saving methods to prepare barley based beverages, such as beer. | ||||||
| 3 | Process for drying malt | US234860 | 1994-04-29 | US5637336A | 1997-06-10 | James R. Kannenberg; Bernard Fulayter |
| A process and apparatus for the drying or kilning of malt in a substantially continuous operation. The malt is transported through one or more separate drying zones by means of fluid bed dryer units at which time tempered or conditioned air at a predetermined temperature and moisture content is passed through the malt to effect a drying of the malt. The rate of malt movement through the drying zones is varied according to the moisture content of the malt at predetermined points in its travel whereby to acheive a desired drying rate and moisture content in the malt as it travels through the various drying zones. Sulfur dioxide gas is selectively infused with the air in the drying zones to minimize carcinogens within the malt. Optional treatments are provided for the malt as it passes through the drying zones, including subjecting the malt to a vacuum to facilitate moisture removal and to effect a sanitizing of the malt. The malt may also be subjected to an irradiation treatment as it moves through the drying zones in order to eliminate insects and other harmful microbes in the malt. | ||||||
| 4 | Malting method and apparatus | JP2003568018 | 2003-02-14 | JP2005517523A | 2005-06-16 | ニコラス，ジェイ． ハリス， |
| 製麦工程を実行するための方法および装置であって、穀粒を容器の底部に近辺から、穀粒の塊の上に上昇され、交流の塊の最上部に再び再分配される容器の底部の中央に導くことによって、底部から最上部への形態で穀粒の塊を効果的にかき混ぜる手段を含む前記方法。 本装置は、製麦工程のいずれの段階にも使用されうる。 | ||||||
| 5 | ENERGY SAVING BREWING METHOD | US15413094 | 2017-01-23 | US20170183611A1 | 2017-06-29 | Søren Knudsen; Preben Riis; Birgitte Skadhauge; Lene Molskov Bech; Ole Olsen |
| Barley based beverages are produced in large quantities, employing highly energy consuming methods, for example in the malting and brewhouse facilities for kiln drying and wort boiling operations, respectively. The present invention relates to energy saving methods for preparing barley based beverages, as well as to barley plants useful in such methods. In particular, the invention describes barley plants with combined traits of null-lipoxygenase-1 (null-LOX-1), null-lipoxygenase-2 (null-LOX-2) and null-S-adenosylmethionine:methionine S-methyltransferase in one plant, which is particularly useful for energy saving methods to prepare barley based beverages, such as beer. | ||||||
| 6 | Energy saving brewing method | US13701604 | 2011-05-31 | US09587210B2 | 2017-03-07 | Søren Knudsen; Preben Riis; Birgitte Skadhauge; Lene Mølskov Bech; Ole Olsen |
| Barley based beverages are produced in large quantities, employing highly energy consuming methods, for example in the malting and brewhouse facilities for kiln drying and wort boiling operations, respectively. The present invention relates to energy saving methods for preparing barley based beverages, as well as to barley plants useful in such methods. In particular, the invention describes barley plants with combined traits of null-lipoxygenase-1 (null-LOX-1), null-lipoxygenase-2 (null-LOX-2) and null-S-adenosylmethionine:methionine S-methyltransferase in one plant, which is particularly useful for energy saving methods to prepare barley based beverages, such as beer. | ||||||
| 7 | METHOD AND APPARATUS FOR KILN DRYING OF MATERIAL FOR KILN DRYING | US14416440 | 2013-06-20 | US20150201651A1 | 2015-07-23 | Kai Silbermann; Detlef Reinberg; Matthias Benz |
| The invention relates to a method for kiln drying of material for kiln drying or kilning material, especially cereals, pseudocereals, oilseeds or legumes, and to an apparatus especially for conduction of the method, wherein the method includes, as process steps, provision of kilning material to be treated on a tray (20) having at least one opening (21) for formation of a layer of kilning material (D) and the production of a gas flow, especially of an air flow (L), and wherein the gas flow, especially the air flow (L), through the layer of kilning material (D) is generated from a space (X) facing the layer of kilning material (D) in the tray (20) having at least one opening (21) to a space (Y) facing away from the layer of kilning material (D) in the tray (20). | ||||||
| 8 | Process and apparatus for kiln-drying malt | US350300 | 1989-05-05 | US4982511A | 1991-01-08 | Willi Frei |
| In the process and apparatus for kiln-drying of malt, at least two zones (A and B) are provided for preliminary drying and one zone (A1) is provided for secondary drying and/cooling of the malt. The unsaturated exhaust air from the secondary drying and/or cooling zone (A1) is admixed as return air with the intake air system, while in the preliminary drying zones (A and B) respectively different preliminary drying times are achieved by the degree of their loading with malt, the design of the floor surface and/or by adjusting the volume flow, the temperature and/or the moisture content of the intake air, so that during the secondary drying in the secondary drying zone (A1), a predrying process is always in operation in at least one predrying zone (A or B). Each individual zone (A, B and A1) is separated in operation as to air technology from the others. The floor surface of a single floor kiln-drier (12) is subdivided by partition walls (26) into three zones (A, B and A1) and the air supply is designed so that the exhaust air is extracted unmixed zone by zone. The partition walls (26) are arranged so that each zone (A, B and A1) has a charging and discharging device (14), or the zones can be rotated into the area of a common charging and discharging device (14). | ||||||
| 9 | Rotary malting equipment | US61157156 | 1956-09-24 | US2947669A | 1960-08-02 | GRAFF ALAN R; JUERGENS EDWIN C; BERKENBLIT SAMUEL E |
| 10 | Method and device for drying malt kiln | JP11718189 | 1989-05-09 | JPH0213353A | 1990-01-17 | BUIRII FURAI |
| PURPOSE: To always execute a predrying process inside predrying bands more than one during secondary drying bands by letting bands for secondary drying and cooling more than two exist as bands for predrying. CONSTITUTION: The bands more than two for predrying and one band for secondary drying or cooling of malt are provided, and non-saturated air discharged from the secondary drying and/or cooling band is mixed as return air with an air in-take system. The respectively different numbers of times of predrying in the predrying bands are achieved corresponding to degrees to fill the inside of these bands with malt, the design on the surface of the floor, the control of volumetric flow, the temperature of in-taken air and the quantity of contained humidity so that the predrying process can be always executed in the predrying bands more than one during secondary drying in the secondary drying band. Besides, ventilation is separated for each band. COPYRIGHT: (C)1990,JPO | ||||||
| 11 | Method and apparatus for continuously producing maltose from grain | JP11720983 | 1983-06-30 | JPS5917975A | 1984-01-30 | BUIRI FURAI |
| 12 | Vertical type malt drying kiln | JP2209985 | 1985-02-08 | JPS60243475A | 1985-12-03 | KURISUCHIYAN KONRATSUDO NAMUBE |
| 13 | JPS5088247A - | JP11039174 | 1974-09-25 | JPS5088247A | 1975-07-15 | |
| 14 | Method and apparatus for kiln drying of material for kiln drying | US14416440 | 2013-06-20 | US09456623B2 | 2016-10-04 | Kai Silbermann; Detlef Reinberg; Matthias Benz |
| The invention relates to a method for kiln drying of material for kiln drying or kilning material, especially cereals, pseudocereals, oilseeds or legumes, and to an apparatus especially for conduction of the method, wherein the method includes, as process steps, provision of kilning material to be treated on a tray (20) having at least one opening (21) for formation of a layer of kilning material (D) and the production of a gas flow, especially of an air flow (L), and wherein the gas flow, especially the air flow (L), through the layer of kilning material (D) is generated from a space (X) facing the layer of kilning material (D) in the tray (20) having at least one opening (21) to a space (Y) facing away from the layer of kilning material (D) in the tray (20). | ||||||
| 15 | Method and apparatus for malting | US10504781 | 2003-02-14 | US20050170043A1 | 2005-08-04 | Nicholas Harris |
| A method and apparatus for carrying out a malting process comprising means for efficiently turning over the grain mass in a bottom to top fashion by directing grain from adjacent to the bottom of the vessel to the centre of the bottom of the vessel from where it is elevated above the grain mass and redistributed back on top of the grain mass. The apparatus can be used for any stage of the malting process. | ||||||
| 16 | Systems for drying malt | US872253 | 1997-06-10 | US6070520A | 2000-06-06 | James R. Kannenberg; Bernard Fulayter |
| A process and apparatus for the drying or kilning of malt in a substantially continuous operation. The malt is transported through one or more separate drying zones by means of fluid bed dryer units at which time tempered or conditioned air at a predetermined temperature and moisture content is passed through the malt to effect a drying of the malt. The rate of malt movement through the drying zones is varied according to the moisture content of the malt at predetermined points in its travel whereby to achieve a desired drying rate and moisture content in the malt as it travels through the various drying zones. Sulfur dioxide gas is selectively infused with the air in the drying zones to minimize carcinogens within the malt. Optional treatments are provided for the malt as it passes through the drying zones, including subjecting the malt to a vacuum to facilitate moisture removal and to effect a sanitizing of the malt. The malt may also be subjected to an irradiation treatment as it moves through the drying zones in order to eliminate insects and other harmful microbes in the malt. | ||||||
| 17 | Vertical maltdrying kiln | US699407 | 1985-02-07 | US4619606A | 1986-10-28 | Christian K. Numberger |
| A vertical maltdrying kiln is described whereby several flow zones for the drying air are provided within a vertical malt compartment. At least in the uppermost flow zone at least one airduct with perforated sidewalls is provided, which extends in the transverse direction through the malt compartment. In the uppermost flow zone, the drying air enters through this airduct and optionally through perforated sidewalls in the transverse direction, while it escapes in the upward direction. Preferrably, a lower malt discharge lock is perforated, so that drying air may enter into the lowermost flow zone. This drying air may escape through perforated sidewalls or through airducts with perforated sidewalls. Preferrably, the entire drying air of all flow zones may escape in the upward direction through the upper open end of the malt compartment. | ||||||
| 18 | Methods and apparatus for the preparation of pale malt | US581165 | 1975-05-27 | US4020562A | 1977-05-03 | Heinz Weyermann |
| Green malt is withered in a stream of humidified air heated to a temperature not greater than 60.degree. C. and thereafter dried in a stream of air at a temperature of up to 85.degree. C. to produce pale malt, in apparatus including a drying kiln, a temperature sensor in the outlet stream of air from said kiln, and a valve operable by the temperature sensor to recycle at least part of said outlet stream of air from said kiln to the air inlet of said kiln. | ||||||
| 19 | Malting of barley and other cereals | US21817062 | 1962-08-20 | US3141833A | 1964-07-21 | BANK LIMITED LLOYDS |
| 20 | Runder Behälter zur Aufnahme von feuchten, aggressiven Stoffen, insbesondere von Weich-, Keim- und Darreinrichtungen in Mälzereien | EP91103027.8 | 1991-02-28 | EP0471143B1 | 1995-08-09 | Hauner, Rudolf, Dipl.-Ing. |
QQ群二维码
意见反馈
意见反馈