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    METHOD FOR TREATING GLYCOL-CONTAINING WELL STREAMS
    13.
    发明申请
    METHOD FOR TREATING GLYCOL-CONTAINING WELL STREAMS 审中-公开
    用于处理含有含糖的含水流的方法

    公开(公告)号：WO2014085065A2

    公开(公告)日：2014-06-05

    申请号：PCT/US2013/069385

    申请日：2013-11-11

    Applicant: DOW GLOBAL TECHNOLOGIES LLC

    Inventor： GOLTZ, H. Robert ,  JOHNSON, Aaron M.

    IPC: C10G5/04

    CPC classification number: C10G5/04 ,  B01D15/362 ,  B01J39/05 ,  B01J49/53 ,  C02F2001/425 ,  C02F2101/34 ,  C02F2103/10 ,  C10G21/16

    Abstract: A continuous method for treating a well stream from natural gas or petroleum production comprising the steps of: i) recovering the well stream from a natural gas or petroleum formation wherein the well stream comprises mono and divalent salts including scale-forming cations, ii) adding glycol to the well stream to form a glycol mixture, iii) heating the glycol mixture to a temperature of at least 35C, iv) passing the glycol mixture through a packed bed of strong acid ion exchange resin to remove at least a portion of the scale forming cations and to form a softened effluent, v) removing at least a portion of water present in the effluent to precipitate monovalent salts, and vi) repeating steps i) through v) and reusing at least a portion of the glycol from step v) in step ii).

    Abstract translation: 一种用于从天然气或石油生产处理井流的连续方法，包括以下步骤：i）从天然气或石油地层回收井流，其中井流包含单价和二价盐，包括水垢形成阳离子，ii）加入 乙二醇以形成二醇混合物，iii）将二醇混合物加热到至少35℃的温度，iv）使二醇混合物通过强酸离子交换树脂的填充床，以除去至少一部分比例 形成阳离子并形成软化的流出物，v）除去存在于流出物中的至少一部分水以沉淀出一价盐，和vi）重复步骤i）至v）并重新使用来自步骤v）的至少一部分二醇， 在步骤ii）中。

    MANNOSE PRODUCTION FROM PALM KERNEL MEAL USING SIMULATED MOVING BED SEPARATION
    14.
    发明申请
    MANNOSE PRODUCTION FROM PALM KERNEL MEAL USING SIMULATED MOVING BED SEPARATION 审中-公开
    使用模拟移动床分离从PALM KERNEL MEAL的MANNOSE生产

    公开(公告)号：WO2014025560A1

    公开(公告)日：2014-02-13

    申请号：PCT/US2013/052351

    申请日：2013-07-26

    Applicant: OROCHEM TECHNOLOGIES, INC.

    Inventor： OROSKAR, Anil R. ,  SUDHARSAN, Naveen S. ,  OROSKAR, Priyana Anil ,  KULKARNI, Omkar M.

    IPC: C12P19/02 ,  C12M1/12

    CPC classification number: C07H3/02 ,  B01D1/26 ,  B01D15/1821 ,  B01D15/185 ,  B01D15/362 ,  B01D61/58 ,  B01D2311/2623 ,  B01D2311/2673 ,  B01J39/05 ,  B01J47/026 ,  B01J49/12 ,  C07H1/08 ,  C12P19/02 ,  C13K1/10 ,  C13K7/00 ,  C13K13/007

    Abstract: Disclosed is a process for the production of d-mannose from fermented palm oil kernel meal using a continuous SMB separation process. The process is useful for providing a simplified processing route to providing high purity d-mannose. The SMB process and the SMB cycle was operated to provide a high purity mannose stream comprising d-mannose, salts, and color agents, a primary raffinate comprising glucose, other sugars and salts, and a secondary raffinate consisting essentially of the mobile phase desorbent. In the SMB cycle, the secondary raffinate was recycled to the SMB process as the mobile phase desorbent without further desalination. The highly pure mannose stream was further treated to remove color agents and salts prior to subsequent steps of precipitation or crystallization and drying. D-mannose is useful as a food additive, as a sweetener, as a texturizer, as a stabilizer, or as a humectant.

    Abstract translation: 公开了一种使用连续的SMB分离方法从发酵的棕榈油籽粒中生产D-甘露糖的方法。 该方法可用于提供简化的处理途径以提供高纯度的D-甘露糖。 操作SMB方法和SMB循环以提供包含D-甘露糖，盐和着色剂的高纯度甘露糖流，包含葡萄糖，其它糖和盐的初级提余液和基本上由流动相解吸剂组成的二级萃余液。 在SMB循环中，作为流动相解吸剂而将二次萃余液再循环至SMB方法，而不再进一步脱盐。 在随后的沉淀或结晶和干燥步骤之前，进一步处理高纯度甘露糖流以除去着色剂和盐。 D-甘露糖可用作食品添加剂，甜味剂，增白剂，稳定剂或湿润剂。

    PROCESSES FOR THE RECOVERY OF URANIUM FROM WET-PROCESS PHOSPHORIC ACID USING A SINGLE DUAL OR DUAL SINGLE CYCLE ION EXCHANGE APPROACHES
    15.
    发明申请
    PROCESSES FOR THE RECOVERY OF URANIUM FROM WET-PROCESS PHOSPHORIC ACID USING A SINGLE DUAL OR DUAL SINGLE CYCLE ION EXCHANGE APPROACHES 审中-公开
    使用单一或双单循环离子交换方法从湿法处理磷酸中恢复铀的工艺

    公开(公告)号：WO2014018422A1

    公开(公告)日：2014-01-30

    申请号：PCT/US2013/051417

    申请日：2013-07-21

    Applicant: K-TECHNOLOGIES, INC.

    Inventor： BERRY, William, W. ,  BAROODY, Thomas, E.

    IPC: C01B25/238 ,  B01J39/04 ,  C01G43/01 ,  C22B60/02

    CPC classification number: C22B60/0265 ,  B01J39/05 ,  B01J45/00 ,  B01J49/00 ,  B01J49/06 ,  B01J49/50 ,  B01J49/53 ,  C01B25/238 ,  C01G43/003 ,  C01G43/01 ,  C22B3/42 ,  C22B3/44 ,  C22B60/0204 ,  C22B60/0217 ,  C22B60/0243 ,  C22C28/00

    Abstract: In alternative embodiments, the invention provides processes and methods for the recovery, removal or extracting of, and subsequent purification of uranium from a wet- process phosphoric acid using a continuous ion exchange processing approach, where the uranium is recovered from a phosphoric acid, or a phos-acid feedstock using either a dual or a single stage extraction methodology. In both cases an intermediate ammonium uranyl-tricarbonate solution is formed. In alternative embodiments, in the dual cycle approach, this solution is contacted in a second continuous ion exchange system with a strong anion exchange resin then subsequently recovered as an acidic uranyl solution that is further treated to produce an intermediate uranyl peroxide compound which is ultimately calcined to produce the final uranium oxide product. In alternative embodiments, in the single cycle case, the intermediate ammonium uranyl-tricarbonate solution is evaporated to decompose the ammonium carbonate and produce an intermediate uranium carbonate/oxide solid material. These solids are digested in an acid medium, and then processed in the same manner as the secondary regeneration solution from the dual cycle process to produce an intermediate uranyl peroxide that is calcined to produce a final uranium oxide product.

    Abstract translation: 在替代实施例中，本发明提供了使用连续离子交换处理方法从湿法磷酸回收，除去或提取和随后纯化铀的方法和方法，其中铀从磷酸中回收，或 使用双级或单级萃取方法的磷酸原料。 在这两种情况下，形成中间铀 - 三碳酸二烷基酯溶液。 在替代实施方案中，在双循环方法中，该溶液在第二连续离子交换系统中与强阴离子交换树脂接触，然后随后作为酸性铀酰溶液回收，其进一步处理以产生最终煅烧的中间体铀酰过氧化物 以生产最终的铀氧化物产品。 在替代实施方案中，在单循环情况下，蒸发中间铀 - 碳酸三烷基酯溶液以分解碳酸铵并产生中间体铀碳酸盐/氧化物固体材料。 这些固体在酸性介质中消化，然后以与来自双循环过程的二次再生溶液相同的方式进行处理，以生产中间体二烷基过氧化物，其被煅烧以产生最终的铀氧化物产物。

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