Process for the Recycling of Expanded Polystyrene
    1.
    发明申请
    Process for the Recycling of Expanded Polystyrene 有权
    膨胀聚苯乙烯回收方法

    公开(公告)号:US20080221228A1

    公开(公告)日:2008-09-11

    申请号:US11996075

    申请日:2006-06-28

    IPC分类号: C08J11/08

    摘要: The invention relates to an enhanced process for the recycling of expanded polystyrene. Said process essentially comprises the reduction in volume of expanded polystyrene by means of dissolution in a solvent, separation of the insoluble components, selective precipitation of the polystyrene with an anti-solvent, separation, drying and extrusion of the precipitated polystyrene, recovery by distillation and recycling of the solvent. The process is characterized in that the anti-solvent is a butanol selected form n-butanol, iso-butanol or sec-butanol and the solvent is dimethyl carbonate, alone or in a mixture containing up to 25% by weight of butanol.

    摘要翻译: 本发明涉及一种用于再发泡聚苯乙烯的增强方法。 所述方法基本上包括通过在溶剂中的溶解减少发泡聚苯乙烯的体积,分离不溶组分,用抗溶剂选择性沉淀聚苯乙烯,分离,干燥和挤出沉淀的聚苯乙烯,通过蒸馏回收和 回收溶剂。 该方法的特征在于,反溶剂是选自正丁醇,异丁醇或仲丁醇的丁醇,溶剂是单独的碳酸二甲酯或含至多25重量%丁醇的混合物。

    Process for the recycling of expanded polystyrene
    2.
    发明授权
    Process for the recycling of expanded polystyrene 有权
    膨胀聚苯乙烯回收工艺

    公开(公告)号:US07728047B2

    公开(公告)日:2010-06-01

    申请号:US11996075

    申请日:2006-06-28

    IPC分类号: C08J11/04

    摘要: The invention relates to an enhanced process for the recycling of expanded polystyrene. Said process essentially comprises the reduction in volume of expanded polystyrene by means of dissolution in a solvent, separation of the insoluble components, selective precipitation of the polystyrene with an anti-solvent, separation, drying and extrusion of the precipitated polystyrene, recovery by distillation and recycling of the solvent. The process is characterized in that the anti-solvent is a butanol selected form n-butanol, iso-butanol or sec-butanol and the solvent is dimethyl carbonate, alone or in a mixture containing up to 25% by weight of butanol.

    摘要翻译: 本发明涉及一种用于再发泡聚苯乙烯的增强方法。 所述方法基本上包括通过在溶剂中的溶解减少发泡聚苯乙烯的体积,分离不溶组分,用抗溶剂选择性沉淀聚苯乙烯,分离,干燥和挤出沉淀的聚苯乙烯,通过蒸馏回收和 回收溶剂。 该方法的特征在于,反溶剂是选自正丁醇,异丁醇或仲丁醇的丁醇,溶剂是单独的碳酸二甲酯或含至多25重量%丁醇的混合物。

    Process for the production of high-purity dimethyl carbonate
    5.
    发明授权
    Process for the production of high-purity dimethyl carbonate 有权
    生产高纯度碳酸二甲酯的方法

    公开(公告)号:US09006476B2

    公开(公告)日:2015-04-14

    申请号:US13508171

    申请日:2010-10-29

    IPC分类号: C07C68/08 C07C69/96

    CPC分类号: C07C68/08 C07C69/96

    摘要: A process for producing a high-purity dimethyl carbonate, which includes: (I) cooling a commercial grade dimethyl carbonate containing 1 ppm or more of chlorine to a temperature from +6° C. to −5° C. at a rate from 0.5-2° C./hour, to obtain a first solid dimethyl carbonate; (II) heating the first solid dimethyl carbonate to a temperature from −5° C. to +6° C. at a rate of 1-5° C./hour, to obtain a mixture comprising a second solid dimethyl carbonate and a predetermined amount of a first liquid dimethyl carbonate; (III) separating the first liquid dimethyl carbonate from the mixture, to obtain the second solid dimethyl carbonate; (IV) heating the second solid dimethyl carbonate to a temperature from 20° C. to 40° C., to obtain a second liquid dimethyl carbonate, wherein the second liquid dimethyl carbonate has a purity degree higher than 99.99% and a chlorine content lower than or equal to 1 ppm.

    摘要翻译: 一种生产高纯度碳酸二甲酯的方法,其包括:(I)以0.5的速度将含有1ppm或更多氯的商业级碳酸二甲酯冷却至+ 6℃至-5℃的温度 -2℃/小时,得到第一固体碳酸二甲酯; (II)以1-5℃/小时的速度将第一固体碳酸二甲酯加热至-5℃至+ 6℃的温度,以获得包含第二固体碳酸二甲酯和预定的 第一液体碳酸二甲酯的量; (III)从混合物中分离第一液体二甲基碳酸酯,得到第二固体碳酸二甲酯; (IV)将第二固体碳酸二甲酯加热至20℃至40℃的温度,得到第二液体碳酸二甲酯,其中第二液体碳酸二甲酯的纯度高于99.99%,氯含量较低 大于等于1ppm。

    PROCESS FOR THE PRODUCTION OF HIGH-PURITY DIMETHYL CARBONATE
    6.
    发明申请
    PROCESS FOR THE PRODUCTION OF HIGH-PURITY DIMETHYL CARBONATE 有权
    生产高纯二甲基碳酸酯的方法

    公开(公告)号:US20120283464A1

    公开(公告)日:2012-11-08

    申请号:US13508171

    申请日:2010-10-29

    IPC分类号: C07C68/08 C07C69/96

    CPC分类号: C07C68/08 C07C69/96

    摘要: A process for producing a high-purity dimethyl carbonate, which includes: (I) cooling a commercial grade dimethyl carbonate containing 1 ppm or more of chlorine to a temperature from +6° C. to −5° C. at a rate from 0.5-2° C./hour, to obtain a first solid dimethyl carbonate; (II) heating the first solid dimethyl carbonate to a temperature from −5° C. to +6° C. at a rate of 1-5° C./hour, to obtain a mixture comprising a second solid dimethyl carbonate and a predetermined amount of a first liquid dimethyl carbonate; (III) separating the first liquid dimethyl carbonate from the mixture, to obtain the second solid dimethyl carbonate; (IV) heating the second solid dimethyl carbonate to a temperature from 20° C. to 40° C., to obtain a second liquid dimethyl carbonate, wherein the second liquid dimethyl carbonate has a purity degree higher than 99.99% and a chlorine content lower than or equal to 1 ppm.

    摘要翻译: 一种生产高纯度碳酸二甲酯的方法,其包括:(I)以0.5的速度将含有1ppm或更多氯的商业级碳酸二甲酯冷却至+ 6℃至-5℃的温度 -2℃/小时,得到第一固体碳酸二甲酯; (II)以1-5℃/小时的速度将第一固体碳酸二甲酯加热至-5℃至+ 6℃的温度,以获得包含第二固体碳酸二甲酯和预定的 第一液体碳酸二甲酯的量; (III)从混合物中分离第一液体二甲基碳酸酯,得到第二固体碳酸二甲酯; (IV)将第二固体碳酸二甲酯加热至20℃至40℃的温度,得到第二液体碳酸二甲酯,其中第二液体碳酸二甲酯的纯度高于99.99%,氯含量较低 大于等于1ppm。

    Process for the synthesis of dimethylcarbonate
    7.
    发明授权
    Process for the synthesis of dimethylcarbonate 失效
    合成碳酸二甲酯的方法

    公开(公告)号:US5478962A

    公开(公告)日:1995-12-26

    申请号:US391169

    申请日:1995-02-21

    IPC分类号: C07C68/00

    CPC分类号: C07C68/005

    摘要: Process for the preparation of dimethylcarbonate which consists in feeding oxygen and a mixture of methanol and carbon monoxide to the reactor, with a molar ratio methanol/carbon monoxide of between 1 and 2, this mixture coming directly from the non catalytic direct oxidation of methane with oxygen characterized in that the above molar ratio between methanol and carbon monoxide, with fixed temperature and pressure values, is obtained by maintaining the ratio between methane and oxygen between 1 and 100, by injections of fresh oxygen into a tubular reactor, during the above oxidation reaction.

    摘要翻译: 制备碳酸二甲酯的方法,其中包括将氧气和甲醇和一氧化碳的混合物进料到反应器中,甲醇/一氧化碳的摩尔比在1和2之间,该混合物直接来自甲烷的非催化直接氧化, 氧气,其特征在于通过在上述氧化过程中通过将新鲜氧气注射到管式反应器中,通过将甲烷与氧气之间的比例保持在1和100之间来获得具有固定温度和压力值的甲醇和一氧化碳之间的上述摩尔比 反应。