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1. 发明申请

US20080220138A1 Process and Equipment to Deactivate Grains 审中-公开
标题翻译：过程和设备去除谷物
公开(公告)号：US20080220138A1
公开(公告)日：2008-09-11
申请号：US11913733
申请日：2006-11-10
申请人： Alcir Dallagnol , Ari Osvaldo Baldus
发明人： Alcir Dallagnol , Ari Osvaldo Baldus
IPC分类号： A23L1/01 , A23L1/10
CPC分类号： A23B9/02 , A23B9/025 , A23B9/08 , A23B9/32
摘要： The aim of this patent is a basically cylindrical vertical body where the displacement of grains occurs through gravity.It is constituted by an antechamber (01) through which the grains enter and are pre-heated when they come in contact with an amount of parallel tubes (02), heated by steam. In the lower part of the chamber (01), there is an entry rotational valve (11) through which the grains pass to the heating chamber (18).Inside the heating chamber (18), there are diverse diametral gutters (14) arranged in opposite positions, with “V” inverted shape walls through which steam is injected into the heating chamber (18) that has a multiple rotational valve of the base (19) in its lower part over the cylinder of the plates (21) heated by steam, where there is an upper heated (22), second (27) and third (28) plates upon which rotational paddles (25) turn that make the grains fall through an opening (26) and a download gutter (32) in the upper one and second plate, and there is a lower rotational valve (31) under the third one.
摘要翻译：该专利的目的是基本上是圆柱体的垂直体，其中颗粒的位移通过重力发生。它由一个前厅（01）构成，通过这个前室（01），当谷物与一定数量的由蒸汽加热的平行管（02）接触时，颗粒进入并预热。在腔室（01）的下部，有一个入口旋转阀（11），颗粒通过该入口旋转阀通过加热室（18）。在加热室（18）的内部，在相对位置上设置有不同的直径槽（14），其中“V”个倒置的壁，蒸汽注入到具有基座的多个旋转阀的加热室（18）中 19）在其被蒸汽加热的板（21）的圆柱体的下部，其中存在旋转桨（25）转动的上部加热（22），第二（27）和第三（28）板，所述上部加热（22），第二（27）和第三（28）颗粒通过上部第一和第二板中的开口（26）和下游沟槽（32）落下，并且在第三板下方具有下旋转阀（31）。

2. 发明申请

US20070010681A1 Process for the production of biodiesel in continuous mode without catalysts 失效
标题翻译：无催化剂连续生产生物柴油的方法
公开(公告)号：US20070010681A1
公开(公告)日：2007-01-11
申请号：US11477451
申请日：2006-06-30
申请人： Alcir Dall'Agnol , Ari Osvaldo Baldus , Claudio Dariva , Eloi Nascimento Sobrinho , Jose Vladimir De Oliveira
发明人： Alcir Dall'Agnol , Ari Osvaldo Baldus , Claudio Dariva , Eloi Nascimento Sobrinho , Jose Vladimir De Oliveira
IPC分类号： C07C51/43
CPC分类号： C10L1/026 , C10G2300/1011 , C11C1/005 , Y02E50/13 , Y02P30/20
摘要： A continuous, non catalytic process for producing biodiesel from vegetable oils and ethanol or methanol includes pumping a mixture of vegetable alcohol through a pump towards a tube shaped reactor, wherein the mixture is submitted to high pressure and temperature, where the resulting product is non reacted alcohol, glycerin and a mixture of esters (biodiesel) which is directed to the reservoir at the reactor outlet where an upper phase of alcohol is redirected through an alcohol return pipe to the pump inlet, and the intermediate phase, biodiesel, and the lower phase (mostly of glycerin) are led to the separation reservoir or decantation tank, where the alcohol is removed through the alcohol return pipe, being biodiesel and glycerin the final products, which are then collected for the end to which they were aimed.
摘要翻译：从植物油和乙醇或甲醇生产生物柴油的连续的非催化方法包括将植物醇的混合物泵送到管状反应器中，其中混合物经受高压和高温，其中所得产物不反应醇，甘油和酯（生物柴油）的混合物，其被引导到反应器出口处的储存器，其中醇的上部相位通过醇返回管重新引导到泵入口，以及中间相，生物柴油和下相（主要是甘油）被引导到分离容器或倾析罐，其中通过酒精回流管除去醇，作为最终产物的生物柴油和甘油，然后将其收集到其目标的末端。

3. 发明授权

US07524982B2 Process for the production of biodiesel in continuous mode without catalysts 失效
标题翻译：无催化剂连续生产生物柴油的方法
公开(公告)号：US07524982B2
公开(公告)日：2009-04-28
申请号：US11477451
申请日：2006-06-30
申请人： Alcir Dall'Agnol , Ari Osvaldo Baldus , Cláudio Dariva , Elói Ricardo Nascimento Sobrinho , José Vladimir De Oliveira
发明人： Alcir Dall'Agnol , Ari Osvaldo Baldus , Cláudio Dariva , Elói Ricardo Nascimento Sobrinho , José Vladimir De Oliveira
IPC分类号： C07C51/43
CPC分类号： C10L1/026 , C10G2300/1011 , C11C1/005 , Y02E50/13 , Y02P30/20
摘要： A continuous, non catalytic process for producing biodiesel from vegetable oils and ethanol or methanol includes pumping a mixture of vegetable alcohol through a pump towards a tube shaped reactor, wherein the mixture is submitted to high pressure and temperature, where the resulting product is non reacted alcohol, glycerin and a mixture of esters (biodiesel) which is directed to the reservoir at the reactor outlet where an upper phase of alcohol is redirected through an alcohol return pipe to the pump inlet, and the intermediate phase, biodiesel, and the lower phase (mostly of glycerin) are led to the separation reservoir or decantation tank, where the alcohol is removed through the alcohol return pipe, being biodiesel and glycerin the final products, which are then collected for the end to which they were aimed.
摘要翻译：从植物油和乙醇或甲醇生产生物柴油的连续的非催化方法包括将植物醇的混合物泵送到管状反应器中，其中混合物经受高压和高温，其中所得产物不反应醇，甘油和酯（生物柴油）的混合物，其被引导到反应器出口处的储存器，其中醇的上部相位通过醇返回管重新引导到泵入口，以及中间相，生物柴油和下相（主要是甘油）被引导到分离容器或倾析罐，其中通过酒精回流管除去醇，作为最终产物的生物柴油和甘油，然后将其收集到其目标的末端。

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