ポリマーペレットの輸送方法および貯蔵方法
    3.
    发明申请
    ポリマーペレットの輸送方法および貯蔵方法 审中-公开
    运输方法和储存聚合物颗粒的方法

    公开(公告)号:WO2008123149A1

    公开(公告)日:2008-10-16

    申请号:PCT/JP2008/055304

    申请日:2008-03-21

    CPC classification number: C08G64/403 C08G63/89

    Abstract:  吸湿性のポリマーペレットを気力輸送する際に、ポリマーペレットの含水率を増大させることなく簡便な手段で輸送することができるポリマーペレットの輸送方法及びポリマーペレットの貯蔵方法を提供する。  ポリマーペレットを圧力気体流と共に輸送配管を介し気力輸送するポリマーペレットの気力輸送方法であって、ポリマーペレットの気力輸送に用いる気体に含まれる水分量を低減し当該気体の露点を0°C以下に調整する気体除湿工程と、気体除湿工程において露点が0°C以下に調整された気体を圧縮する気体圧縮工程と、気体圧縮工程において圧縮された圧力気体をポリマーペレット1トン当たり50Nm 3 /時間~600Nm 3 /時間で輸送配管内に供給する圧力気体供給工程と、圧力気体供給工程において輸送配管に供給された圧力気体流と共にポリマーペレットを輸送配管を介し気力輸送する輸送工程と、を有することを特徴とするポリマーペレットの気力輸送方法。

    Abstract translation: 输送聚合物颗粒的方法,其中在吸湿聚合物颗粒的气动输送中,可以通过容易的方式进行运输,而不增加聚合物颗粒的含水量; 以及储存聚合物颗粒的相关方法。 涉及将聚合物颗粒与压力气体流动通过输送管道气动输送的气动聚合物颗粒输送的方法的特征在于包括减少聚合物颗粒的气动输送中使用的气体的含水量的气体除湿步骤,以便 将气体的露点调节至0℃以下; 在气体除湿工序中将其露点调节为0℃以下的气体进行压缩的气体压缩工序; 所述压力气体供给步骤以每吨聚合物粒料50〜600Nm 3 / hr的速率在所述输送管道中供给在所述气体压缩工序中被压缩的压力气体; 以及通过聚合物粒料的输送管道进行气动输送的输送步骤,以及在压力气体供给步骤中已经供给到输送管道中的压力气体流。

    PROCESS FOR THE PREPARATION OF POLYMERS FROM POLYMER SLURRIES
    4.
    发明申请
    PROCESS FOR THE PREPARATION OF POLYMERS FROM POLYMER SLURRIES 审中-公开
    聚合物制备聚合物的方法

    公开(公告)号:WO2006088819B1

    公开(公告)日:2007-04-12

    申请号:PCT/US2006005083

    申请日:2006-02-13

    Inventor: IBAR JEAN-PIERRE

    CPC classification number: C08G64/403 C08G63/89 C08L77/06

    Abstract: A process for manufacturing a polymer having a molecular weight in excess of 5,000, and preferably in excess of 40,000, comprises, producing a polymerized reaction mass in which the polymer is dispersed, the reaction mass including solvents), unreacted monomer and other unwanted contaminants; feeding the reaction mass to a means for disentangling the polymer's molecules to produce a modified polymer in the reaction mass; feeding the modified polymer in the reaction mass to a polymer-recovering means; removing the unwanted volatiles and other byproducts; and, recovering a high molecular weight substantially pure modified polymer having substantially the same molecular weight as the polymer fed to the disentangling means and a viscosity at least 10% lower than that of the polymer fed to the disentangling means.

    Abstract translation: 制造分子量超过5,000,优选超过40,000的聚合物的方法包括制备其中分散有聚合物的聚合反应物质,反应物质包括溶剂),未反应的单体和其它不需要的污染物; 将反应物料送入用于解聚聚合物分子的装置以在反应物质中产生改性聚合物; 将反应物质中的改性聚合物进料到聚合物回收装置; 去除不需要的挥发物和其他副产物; 并且回收具有与供给到解缠装置的聚合物基本上相同的分子量的高分子量基本上纯的改性聚合物,并且粘度比供给到解缠装置的聚合物的粘度低至少10%。

    METHOD FOR THE PRODUCTION OF A HOMO- OR COPOLYMER OF A POLY- beta -HYDROXYALKANOIC ACID (PHA) FROM BIOMASS
    6.
    发明申请
    METHOD FOR THE PRODUCTION OF A HOMO- OR COPOLYMER OF A POLY- beta -HYDROXYALKANOIC ACID (PHA) FROM BIOMASS 审中-公开
    PROCEDURE由生物质获得的均聚物或共聚物A的βPOLY-HYDROXYALKANSÄURE(PHA)

    公开(公告)号:WO01034826A1

    公开(公告)日:2001-05-17

    申请号:PCT/EP2000/010442

    申请日:2000-10-20

    CPC classification number: C12P7/625 C08G63/89

    Abstract: The invention relates to a method for the production of a homo- or copolymer of a poly- beta -hydroxyalkanoic acid (PHA) from biomass, characterized in that the biomass is extracted by 1-methyl-2-pyrrolidone (NMP), optionally using a water binding agent, from a viscous suspension which forms at a temperature >/= of 40 DEG C. PHA-containing solution is separated out and PHA is subsequently precipitated out.

    Abstract translation: 本发明涉及一种用于获得从生物质聚-β--hydroxyalkansäure(PHA),其特征在于的均聚物或共聚物,其与1-甲基-2-吡咯烷酮(NMP),任选地添加水结合剂的生物量, 被提取,从在温度> / = 40℃,然后将PHA沉淀所得粘性悬浮液含PHA的溶液中分离。

    METHODS FOR SEPARATION AND PURIFICATION OF BIOPOLYMERS
    7.
    发明申请
    METHODS FOR SEPARATION AND PURIFICATION OF BIOPOLYMERS 审中-公开
    生物聚合物的分离和纯化方法

    公开(公告)号:WO99051760A1

    公开(公告)日:1999-10-14

    申请号:PCT/US1999/007689

    申请日:1999-04-08

    CPC classification number: C08G63/90 C08G63/89

    Abstract: Methods for the recovery and purification of polyhydroxyalkanoates (PHAs) from biomass containing PHAs, wherein the methods include treating the biomass or partially purified PHA with ozone, in at least one step of a purification process, have been developed. Treatment of PHA-containing biomass or partially purified PHA with ozone yields an enhanced level of purity suitable for coating and other applications. The ozone treatment also has the added advantage that the resulting PHA polymer or polymer latex is essentially odor-free. The ozone treatment may be used alone or in combination with other treatment, extraction, and separation stages, and is especially suitable for the treatment of PHA-containing latexes, slurries, suspensions, and organic solutions.

    Abstract translation: 已经开发了用于从包含PHAs的生物质中回收和纯化聚羟基链烷酸酯(PHA)的方法,其中所述方法包括在纯化过程的至少一个步骤中用臭氧处理生物质或部分纯化的PHA。 用臭氧处理含PHA的生物质或部分纯化的PHA产生适于涂层和其它应用的增强的纯度。 臭氧处理还具有附加的优点,即所得PHA聚合物或聚合物胶乳基本上不含气味。 臭氧处理可以单独使用或与其他处理,提取和分离阶段组合使用,特别适用于处理含PHA的胶乳,浆液,悬浮液和有机溶液。

    METHODS FOR ISOLATING POLYHYDROXYALKANOATES FROM PLANTS
    8.
    发明申请
    METHODS FOR ISOLATING POLYHYDROXYALKANOATES FROM PLANTS 审中-公开
    从植物中分离聚羟基烷基化物的方法

    公开(公告)号:WO1997015681A1

    公开(公告)日:1997-05-01

    申请号:PCT/US1996016921

    申请日:1996-10-23

    CPC classification number: C08G63/89 C12P7/625

    Abstract: Methods are provided for separating polyhydroxyalkanoates ("PHAs") from plants, such as transgenic oil crop plants. The methods advantageously permit both the oil and the PHAs to be recovered from the plant biomass. To isolate the PHAs, in one embodiment, a biomass derived from an oil crop plant is pre-processed, for example by grinding, crushing or rolling. The oil then is extracted from the biomass with a first solvent in which the oil is soluble and in which the PHAs are not highly soluble to remove the oil. The biomass then can be extracted with a second solvent in which the PHA is soluble, to separate the PHA from the biomass. Alternatively, the PHA-containing biomass is treated with a chemical or biochemical agent, such as an enzyme, to chemically transform the PHA into a PHA derivative. The PHA derivative then is separated from the mixture using, for example, a physical separation process such as distillation, extraction or chromatography. Advantageously, using the method, the plant oils, the PHAs and PHA derivatives can be recovered and purified on a large scale from oil containing plants such as transgenic oil crop plants.

    Abstract translation: 提供了从植物如转基因油料作物植物中分离聚羟基链烷酸酯(“PHAs”)的方法。 该方法有利地允许从植物生物质中回收油和PHA。 为了分离PHA,在一个实施方案中,来自油料作物植物的生物质被预处理,例如通过研磨,破碎或轧制。 然后用第一溶剂从生物质中提取油,其中油是可溶的,并且其中PHAs不是高度可溶的以除去油。 然后生物质可以用其中PHA可溶的第二溶剂萃取,以将PHA与生物质分离。 或者,将含PHA的生物质用化学或生化剂如酶处理,以将PHA化学转化为PHA衍生物。 然后使用例如物理分离方法如蒸馏,萃取或色谱法将PHA衍生物与混合物分离。 有利地,使用该方法,植物油,PHA和PHA衍生物可以从含油植物如转基因油料作物植物大规模回收和纯化。

    PRODUCING POLYHYDROXYALKANOATE COPOLYMERS FROM ORGANIC WASTE PRODUCTS
    9.
    发明申请
    PRODUCING POLYHYDROXYALKANOATE COPOLYMERS FROM ORGANIC WASTE PRODUCTS 审中-公开
    从有机废物生产聚羟基烷酸酯共聚物

    公开(公告)号:WO2016081902A1

    公开(公告)日:2016-05-26

    申请号:PCT/US2015/061991

    申请日:2015-11-20

    Abstract: Producing a resin from an organic waste product includes assessing a weight percent of a first volatile fatty acid and a weight percent of a second volatile fatty acid in a liquid mixture having volatile fatty acids from the organic waste product. The weight percent of the volatile fatty acids is based on the total weight of the carboxylic acids in the liquid mixture, the total weight of volatile fatty acids in the liquid mixture, or the total weight of lactic acid and volatile fatty acids in the mixture. A ratio of the weight percent of the first volatile fatty acid to the weight percent of the second volatile fatty acid in the liquid mixture is adjusted to yield a modified liquid mixture. The modified liquid is combined with polyhydroxyalkanoate-producing bacteria to yield a polyhydroxyalkanoate copolymer; and the polyhydroxyalkanoate copolymer is extracted from the polyhydroxyalkanoate-producing bacteria.

    Abstract translation: 从有机废物产生树脂包括在具有来自有机废物的挥发性脂肪酸的液体混合物中评估第一挥发性脂肪酸的重量百分数和第二挥发性脂肪酸的重量百分比。 挥发性脂肪酸的重量百分比是基于液体混合物中羧酸的总重量,液体混合物中挥发性脂肪酸的总重量,或混合物中乳酸和挥发性脂肪酸的总重量。 调节液体混合物中第一挥发性脂肪酸的重量百分数与第二挥发性脂肪酸的重量百分比的比例,得到改性的液体混合物。 将改性液体与产生聚羟基链烷酸酯的细菌结合产生聚羟基链烷酸酯共聚物; 从聚羟基链烷酸酯生产菌中提取聚羟基链烷酸酯共聚物。

    CRYSTALLIZED PELLET/LIQUID SEPARATOR
    10.
    发明申请
    CRYSTALLIZED PELLET/LIQUID SEPARATOR 审中-公开
    结晶泡沫/液体分离器

    公开(公告)号:WO2007037968A3

    公开(公告)日:2010-09-02

    申请号:PCT/US2006035364

    申请日:2006-09-13

    Abstract: A process and apparatus which reduces the fines in a liquid discharge stream and/or increases the dryness of a solids discharge stream while under a pressure equal to or greater than the vapor pressure of the liquid. There is provided a process for separating particles such as polyethylene terephthalate or polyethylene naphthalate from a liquid in a slurry comprising: a. feeding a slurry comprising solid particles and a liquid into a within a separation zone maintained at a pressure equal to or greater than the vapor pressure of the liquid; b. contacting the slurry in the separation zone with a porous filter, optionally a microfilter, nanofilter, reverse osmosis filter, or ultrafilter, and separating liquid from the particles, wherein the liquid flows through the filter into an outer annulus defined as a space between the wall of the separation device and the filter, and said porous filter optionally having a terminal point beyond which the separated liquid does not pass from the outer annulus back through the filter; c. accumulating no liquid in the outer annulus or accumulating liquid in the outer annulus at a level below or in front of the terminal point, and continuously discharging the separated liquid from the outer annulus through a liquid outlet; d. decoupling the particles from the separation zone through the solids outlet to a low pressure below the vapor pressure of the liquid at the liquid temperature within the separation zone while maintaining a pressure on the particles prior to decoupling at or above the vapor pressure of the liquid within the separation zone.

    Abstract translation: 一种在液体排出流中减少细粉和/或在等于或大于液体的蒸气压的压力下增加固体排出流的干度的方法和装置。 提供了一种用于从浆液中的液体分离颗粒如聚对苯二甲酸乙二醇酯或聚萘二甲酸乙二醇酯的方法,包括:a。 将包含固体颗粒和液体的浆料进料到保持在等于或大于液体的蒸气压的压力的分离区内; 湾 使分离区中的浆料与多孔过滤器,任选的微过滤器,纳米过滤器,反渗透过滤器或超滤器接触,并将液体从颗粒中分离,其中液体流过过滤器,形成外壁,其被定义为壁之间的空间 分离装置和过滤器,并且所述多孔过滤器任选地具有终点,超过该终点,分离的液体不从外环通过过滤器; C。 在外环形空间中没有液体或在外环空中积聚液体在终点下方或前方的水平,并且通过液体出口连续排出来自外环的分离的液体; 天。 在分离区内的液体温度下将来自分离区的颗粒通过固体出口分离成低于液体蒸气压的低压,同时在等于或高于液体的蒸汽压力的去耦之前保持颗粒上的压力, 分离区。

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