BLOWN CORN STILLAGE OIL
    53.
    发明申请
    BLOWN CORN STILLAGE OIL 有权
    黑色油渍油

    公开(公告)号:US20140275593A1

    公开(公告)日:2014-09-18

    申请号:US14294447

    申请日:2014-06-03

    IPC分类号: C11B3/02

    摘要: Blown corn stillage oils and methods for making blown corn stillage oils are disclosed. In one aspect the corn stillage oils are stripped to reduce the acid value of the resulting blown, stripped corn stillage oil. The method includes heating a corn stillage oil to a temperature of at least 90° C., and passing air through the heated oil to produce a blown corn stillage oil having a viscosity of at least 50 cSt at 40° C. In one aspect, the blown corn stillage oil is stripped to reduce the acid value of the blown, stripped corn stillage oil to 5 mg KOH/gram or less.

    摘要翻译: 公开了吹制的玉米淀粉油和用于制备爆炸的玉米淀粉油的方法。 在一个方面,剥去玉米酒糟油以降低所得吹制,剥离的玉米汤液油的酸值。 该方法包括将玉米釜馏液加热到至少90℃的温度,并使空气通过加热的油,以产生在40℃下具有至少50cSt粘度的吹入的玉米釜渣油。在一个方面, 将吹入的玉米淀粉油去除,将吹制的剥离的玉米汤液的酸值降低至5mg KOH /克或更低。

    Biodiesel automatic titration system
    55.
    发明授权
    Biodiesel automatic titration system 失效
    生物柴油自动滴定系统

    公开(公告)号:US08722413B1

    公开(公告)日:2014-05-13

    申请号:US13214923

    申请日:2011-08-22

    IPC分类号: C11B3/00 C11B3/02

    CPC分类号: C11B3/008

    摘要: An automated system and process for the titration of either Waste vegetable oil (WVO) or virgin vegetable oil during its chemical conversion into Biodiesel. A system capable of automatically measuring and controlling the addition of a suitable amount of titration fluid is controlled in reaction to a pH level measurement tool, as determined by sensors and software. The process comprises forming a single phase solution of WVO and titrant in a ratio of between 10:1 to 50:1.

    摘要翻译: 在化学转化成生物柴油期间将废弃植物油(WVO)或原始植物油滴定的自动化系统和方法。 控制能够自动测量和控制添加适量滴定液的系统,以响应由pH传感器和软件确定的pH值测量工具。 该方法包括以10:1至50:1的比例形成WVO的单相溶液和滴定剂。

    DECANTATION IMPROVEMENT IN A METHOD OF PRODUCING ALKYL ESTERS FROM VEGETABLE OR ANIMAL OIL AND AN ALIPHATIC MONOALCOHOL
    59.
    发明申请
    DECANTATION IMPROVEMENT IN A METHOD OF PRODUCING ALKYL ESTERS FROM VEGETABLE OR ANIMAL OIL AND AN ALIPHATIC MONOALCOHOL 失效
    从蔬菜或动物油和阿拉伯糖醇生产烷基酯的方法中的表征改进

    公开(公告)号:US20100292493A1

    公开(公告)日:2010-11-18

    申请号:US12666885

    申请日:2008-06-09

    IPC分类号: C11B3/02 B01J19/00

    CPC分类号: C11C3/003 C11C3/10 Y02E50/13

    摘要: The present invention describes a method of producing fatty acid alkyl esters and glycerin implementing, in a reaction section, a set of transesterification reactions between a vegetable or animal oil and an aliphatic monoalcohol, and using a heterogeneous solid catalyst, comprising: a) a stage of recontacting the effluent coming from the reaction section, and separated from the excess alcohol, with a glycerin phase, b) a stage of mixing said effluent with said glycerin phase, and c) a glycerin phase decantation stage. The supernatent ester phase obtained after decantation is then optionally sent to a coalescer, also allowing separation of the glycerin, then to a purification stage by adsorption on solids.

    摘要翻译: 本发明描述了一种生产脂肪酸烷基酯和甘油的方法,其在反应部分中实施植物油或动物油与脂族一元醇之间的一组酯交换反应,并使用非均相固体催化剂,其包括:a) 重新反应来自反应段的流出物,并与过量的醇分离出甘油相,b)将所述流出物与所述甘油相混合的阶段,和c)甘油相倾析阶段。 然后将倾析后获得的上清液相可选地送至聚结器,还允许甘油分离,然后通过在固体上吸附进入纯化阶段。

    Cationic polymerization of biological oils with superacid catalysts
    60.
    发明授权
    Cationic polymerization of biological oils with superacid catalysts 有权
    生物油与超酸催化剂的阳离子聚合

    公开(公告)号:US07501479B2

    公开(公告)日:2009-03-10

    申请号:US11800736

    申请日:2007-05-07

    摘要: A method for the cationic polymerization of unsaturated biological oils (e.g., vegetable oils and animal oils) based on the cationic reaction of double bonds initiated by superacids is provided. The process occurs under very mild reaction conditions (about 70-110° C. and atmospheric pressure) and with short reaction times. The polymerized oils have a viscosity about 10 to 200 times higher than the initial oil and relatively high unsaturation (only about 10-30% lower than that of initial oils).

    摘要翻译: 提供了基于由超强酸引发的双键的阳离子反应的不饱和生物油(例如植物油和动物油)的阳离子聚合的方法。 该过程发生在非常温和的反应条件(约70-110℃和大气压)下,反应时间短。 聚合油的粘度比初始油高约10至200倍,并且具有相对高的不饱和度(比初始油低约10-30%)。