会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 2. 发明申请
    • CELLULOSE ACETATE AND PRODUCING METHOD THEREFOR
    • US20190218312A1
    • 2019-07-18
    • US16327054
    • 2017-08-21
    • DAICEL CORPORATION
    • Maiko TSUDAAkihiro HIGUCHI
    • C08B3/06C08B1/02C08B17/02
    • C08B3/06B02C7/16B02C13/04C08B1/02C08B17/02
    • The purpose of the present invention is to provide a cellulose acetate which can be used to obtain an optical film having a very small amount of bright spot foreign matters, with excellent production efficiency, even when cellulose containing a small amount of hemicellulose components and having a high degree of crystallinity is used as a raw material. A cellulose acetate in which a content ratio by mole of mannose units to a sum of xylose units, mannose units and glucose units, which are sugar chain components, is 0.04 mol % or less, and a filtration index K measured by the following measurement method is 30 mL−1 or less. (Measurement method) The cellulose acetate is dissolved in a mixed solvent containing methylene chloride and methanol at a weight ratio of methylene chloride/methanol of 9/1 to obtain a solution with a solid concentration of 16% by weight. The temperature of the solution is adjusted to 25° C., and the solution is subjected to constant-pressure filtration under a pressure of 3 kg/cm2 using a cloth obtained by stacking three sheets of calico (s 618) (diameter: 15 mm, filtration area: 1.77 cm2). At this time, the filtration index k (mL−1) is calculated from the following expression, where P1 represents the amount of filtration (mL) up to 20 minutes after the start of filtration, and P2 represents the amount of filtration (mL) from 0 to 60 minutes. Filtration   index   K = 2 - P 2 / P 1 P 1 + P 2 × 10 4 [ Mathematical   Formula   1 ]
    • 8. 发明申请
    • Method of manufacturing cellulose acetate, high temperature steam reactor vessel used in the same method, and superheated steam generator used in the same method
    • 制造醋酸纤维素的方法,以相同方法使用的高温蒸汽反应器容器和以相同方法使用的过热蒸汽发生器
    • US20070249824A1
    • 2007-10-25
    • US11510725
    • 2006-08-28
    • Teruyuki Shikata
    • Teruyuki Shikata
    • C08B1/02F01N3/10
    • C08B3/06C08B1/02C08B17/02
    • The present invention relates to a method of manufacturing cellulose acetate by use of a high temperature steam reactor vessel and a superheated steam generator. According to this method, a material to which solid catalyst added is subject to a steaming process so as to cause cellulose content to be separated from the material, followed by carrying out an acetylating process of the separated cellulose content together with solid acid in the state of being pressurized so as to obtain cellulose acetate. The high temperature steam reactor vessel employs a system that there is arranged in a reactor vessel body 1 a cartridge 2 filled with collective chips 100, whereby enabling the material subjected to the process to be readily handled and processed, and also resulting in that there is no need to carry out in a later process separation between useful content and residue produced in hydrolysis with high temperature steam. The superheated steam generator comprises a heat-exchange line 3 having line parts P1, P2, P3 sectioned into plural stages and so adapted that a sectional area of the line part on a stage at a downstream side is larger than that of the line part on a stage at an upstream side, whereby superheated steam having ultra high temperature is able to be generated while or although pressure proof properties can be designed to be relatively lower.
    • 本发明涉及使用高温蒸汽反应器容器和过热蒸汽发生器制造乙酸纤维素的方法。 根据该方法,加入固体催化剂的材料进行蒸汽处理,以使纤维素含量与材料分离,然后在该状态下进行分离的纤维素含量与固体酸的乙酰化过程 被加压以获得醋酸纤维素。 高温蒸汽反应堆容器采用在反应器容器主体1中设置有填充有集合芯片100的盒2的系统,由此能够容易地处理和处理经过该处理的材料,并且还导致存在 不需要在稍后的过程中进行有用含量与用高温蒸汽水解产生的残留物之间的分离。 过热蒸汽发生器包括热交换管线3,其具有分段成多级的管线部分P 1,P 2,P 3,并且适于使下游侧的工作台上的管线部分的截面面积大于 在上游侧的台阶上,能够产生具有超高温的过热蒸汽,或者虽然耐压性能可以设计得相对较低。
    • 9. 发明授权
    • Apparatus for acetylating cellulose
    • 纤维素乙酰化装置
    • US5928613A
    • 1999-07-27
    • US92979
    • 1998-06-08
    • Mitsuru Yamashita
    • Mitsuru Yamashita
    • B01J19/00C08B3/06C08B17/02B01J8/04B01J10/00
    • C08B3/06B01J19/0006C08B17/02B01J2219/00162
    • In a production process of a cellulose acetate which comprises (a) a reduced pressure-acetylation step of acetylating a cellulose under a reduced pressure in the presence of sulfuric acid or other acidic catalyst, with distilling off a gaseous phase component of the reaction system out of the system, and (b) a post-acetylation step of allowing the acetylation to further proceed by increasing the pressure as compared with the pressure of the reduced pressure-acetylation step by means of release of the pressure reduction of the reaction system or the like, the shift operation from the reduced pressure-acetylation step to the post-acetylation step is conducted by taking a distilling rate of a distillate in the reduced pressure-acetylation step as an index to control the reaction temperature of the post-acetylation step. The shift operation from the reduced pressure-acetylation step to the post-acetylation step may also be conducted by taking a distilling rate after the distilling rate in the reduced pressure-acetylation step has reached a maximum value.
    • 在乙酸纤维素的生产方法中,其包括(a)在硫酸或其它酸性催化剂存在下,在减压下乙酰化纤维素的减压乙酰化步骤,将反应体系的气相成分蒸出 和(b)通过减轻反应体系的压力降低或减压乙酰化步骤的压力与减压乙酰化步骤相比通过增加压力使乙酰化进一步进行的后乙酰化步骤,或 通过将减压乙酰化步骤中的馏出物的蒸馏速度作为控制后乙酰化步骤的反应温度的指标进行从减压乙酰化步骤到后乙酰化步骤的转移操作。 从减压乙酰化步骤到后乙酰化步骤的转移操作也可以通过在减压 - 乙酰化步骤中的蒸馏速率达到最大值之后进行蒸馏速率。
    • 10. 发明授权
    • Method and apparatus for acetylating cellulose
    • 乙酰化纤维素的方法和装置
    • US5869646A
    • 1999-02-09
    • US787565
    • 1997-01-22
    • Mitsuru Yamashita
    • Mitsuru Yamashita
    • B01J19/00C08B3/06C08B17/02
    • C08B3/06B01J19/0006C08B17/02B01J2219/00162
    • In a production process of a cellulose acetate which comprises (a) a reduced pressure-acetylation step of acetylating a cellulose under a reduced pressure in the presence of sulfuric acid or other acidic catalyst, with distilling off a gaseous phase component of the reaction system out of the system, and (b) a post-acetylation step of allowing the acetylation to further proceed by increasing the pressure as compared with the pressure of the reduced pressure-acetylation step by means of release of the pressure reduction of the reaction system or the like, the shift operation from the reduced pressure-acetylation step to the post-acetylation step is conducted by taking a distilling rate of a distillate in the reduced pressure-acetylation step as an index to control the reaction temperature of the post-acetylation step. The shift operation from the reduced pressure-acetylation step to the post-acetylation step may also be conducted by taking a distilling rate after the distilling rate in the reduced pressure-acetylation step has reached a maximum value.
    • 在乙酸纤维素的生产方法中,其包括(a)在硫酸或其它酸性催化剂存在下,在减压下乙酰化纤维素的减压乙酰化步骤,蒸馏出反应体系的气相成分 和(b)通过减轻反应体系的压力降低或减压乙酰化步骤的压力与减压乙酰化步骤相比通过增加压力使乙酰化进一步进行的后乙酰化步骤,或 通过将减压乙酰化步骤中的馏出物的蒸馏速度作为控制后乙酰化步骤的反应温度的指标进行从减压乙酰化步骤到后乙酰化步骤的转移操作。 从减压乙酰化步骤到后乙酰化步骤的转移操作也可以通过在减压 - 乙酰化步骤中的蒸馏速率达到最大值之后进行蒸馏速率。