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
    • 1. 发明申请
    • DENTAL COMPOSITION
    • US20190209440A1
    • 2019-07-11
    • US16357862
    • 2019-03-19
    • DENTSPLY SIRONA Inc.
    • Joachim KLEE
    • A61K6/087A61K6/00C08G59/50C08G59/32C08G59/06C08L63/00C07D303/23C07D301/16C08G59/24
    • Dental composition comprising (a) at least two di- or polyepoxides having 2 to 5 epoxide groups and having a molecular weight of from 200 to 700 Da, or a macromonomeric reaction product obtainable by reacting the diepoxide with a dicarboxylic acid in a molar ratio [diepoxide]/[dicarboxylic acid] of at least 2; (b) one or more primary monoamines and/or disecondary diamines; (c) optionally one or more aliphatic polyamines; (d) a particulate filler, wherein the molar ratio of epoxide groups in component (a) to the N—H bonds in component (b) and (c) [epoxide(a)]/[N—H(b),(c)] is in the range of from 0.9 to 1.1; wherein the di- or polyepoxide having 2 to 5 epoxide groups is a compound of the following formula (I): A(BZm)n   (I) wherein A represents an n-valent organic moiety optionally having 1 to 10 heteroatoms selected from oxygen atoms and sulfur atoms; and B represents an m+1-valent organic moiety, Z is an epoxide group which may have a substituent, m which are independent from each other represent an integer of at least 1; and n is an integer of from 1 to 5; wherein the m are selected so that 2 to 5 epoxide groups are present; wherein the composition does not contain any 2,2-bis-(4-hydroxyphenyl)-propane, or 2,2-bis-(4-hydroxyphenyl)-methane.
    • 4. 发明授权
    • Continuous process for the catalytic epoxidation of olefinic double
bonds with hydrogen peroxide and formic acid
    • 用过氧化氢和甲酸催化环氧化烯属双键的连续方法
    • US4584390A
    • 1986-04-22
    • US615446
    • 1984-05-30
    • Gerhard DieckelmannKlemens EckwertLutz JerominEberhard PeukertUdo Steinberner
    • Gerhard DieckelmannKlemens EckwertLutz JerominEberhard PeukertUdo Steinberner
    • C07D301/14C07D301/16C07D303/00C07D303/04C07D303/14C07D303/42
    • C07D303/42C07D301/14C07D301/16C07D303/04C07D303/14
    • In a multistage process for the continuous epoxidation of double bonds of terminal and non-terminal olefins containing more than 12 carbon atoms, unsaturated higher fatty acids and their lower alkanol and lower alkanediol esters and also unsaturated fatty alcohols containing from 8 to 18, preferably 18, carbon atoms and triglycerides of higher fatty acids including unsaturated fatty acids, preferably soyabean oil, using performic acid formed in situ from hydrogen peroxide and formic acid, the reactants, olefin and hydrogen peroxide/formic acid, are passed at ambient pressure in cross-counter flow through an at least three-stage reaction cascade. The olefinic phase is introduced into the first reaction stage, the hydrogen peroxide and the formic acid are introduced in separate streams into the penultimate reaction stage and the olefin phase and the hydrogen peroxide/formic acid phase (acid water phase) are separated from one another in a phase separator after each reaction stage. The olefinic phase passes successively through reaction stages I to n while the acid water, after reaction stage (n-1), passes through reaction stages (n-2) to 2 in counter flow to the olefin phase and then through stages n and 1, the reaction temperature being maintained in the range from 50.degree. to 80.degree. C. in the reactors and in the range from 15.degree. to 60.degree. C. in the phase separators.
    • 在用于连续环氧化含有12个以上碳原子的末端和非末端烯烃的双键的多级方法中,不饱和高级脂肪酸及其低级链烷醇和低级链烷二醇酯以及含有8-18个不饱和脂肪醇,优选18个 ,使用由过氧化氢和甲酸原位形成的甲酸,反应物,烯烃和过氧化氢/甲酸的高级脂肪酸的碳原子和甘油三酯,包括不饱和脂肪酸,优选大豆油,在环境压力下通过, 逆流通过至少三级反应级联。 将烯烃相引入第一反应阶段,将过氧化氢和甲酸分别引入倒数第二反应阶段,并将烯烃相和过氧化氢/甲酸相(酸水相)彼此分离 在每个反应阶段之后的相分离器中。 烯烃相依次通过反应段I至n,反应阶段(n-1)之后的酸性水通过反应阶段(n-2)反应到烯烃相,然后通过阶段n和1 ,反应器中的反应温度保持在50〜80℃,相分离器在15〜60℃的范围内。
    • 5. 发明授权
    • Dental composition
    • US10596078B2
    • 2020-03-24
    • US16357862
    • 2019-03-19
    • DENTSPLY SIRONA Inc.
    • Joachim Klee
    • A61K6/087A61K6/00C08G59/50C08G59/32C08G59/24C08G59/06C08L63/00C07D303/23C07D301/16
    • Dental composition comprising (a) at least two di- or polyepoxides having 2 to 5 epoxide groups and having a molecular weight of from 200 to 700 Da, or a macromonomeric reaction product obtainable by reacting the diepoxide with a dicarboxylic acid in a molar ratio [diepoxide]/[dicarboxylic acid] of at least 2; (b) one or more primary monoamines and/or disecondary diamines; (c) optionally one or more aliphatic polyamines; (d) a particulate filler, wherein the molar ratio of epoxide groups in component (a) to the N—H bonds in component (b) and (c) [epoxide(a)]/[N—H(b),(c)] is in the range of from 0.9 to 1.1; wherein the di- or polyepoxide having 2 to 5 epoxide groups is a compound of the following formula (I): A(BZm)n  (I) wherein A represents an n-valent organic moiety optionally having 1 to 10 heteroatoms selected from oxygen atoms and sulfur atoms; and B represents an m+1-valent organic moiety, Z is an epoxide group which may have a substituent, m which are independent from each other represent an integer of at least 1; and n is an integer of from 1 to 5; wherein the m are selected so that 2 to 5 epoxide groups are present; wherein the composition does not contain any 2,2-bis-(4-hydroxyphenyl)-propane, or 2,2-bis-(4-hydroxyphenyl)-methane.
    • 8. 发明授权
    • Process for producing propylene oxide
    • 生产环氧丙烷的方法
    • US5599955A
    • 1997-02-04
    • US605602
    • 1996-02-22
    • Bipin V. VoraPeter R. Pujado
    • Bipin V. VoraPeter R. Pujado
    • C07D301/12C10G3/00C07D301/14C07D301/16
    • C07D301/12C10G3/49B01J21/063B01J29/89C10G2300/1022C10G2300/4081C10G2300/4087C10G2400/20Y02P20/125Y02P20/52
    • The present invention provides an integrated process for the production of propylene oxide from an alternate feedstream such as synthesis gas. In the process, propylene oxide is produced from a feedstream comprising hydrogen and a carbon oxide. A portion of the feedstream is passed to an oxygenate production zone to produce an oxygenate stream comprising methanol and dimethyl ether, and the oxygenate stream is passed to an olefin production zone containing a metal aluminophosphate catalyst to produce a propylene stream. The propylene stream is epoxidized with hydrogen peroxide which has been produced from hydrogen separated from a portion of the feedstream. The spent water stream produced by the epoxidation reaction is treated to remove heavy components and returned to the hydrogen peroxide production zone. The return of the unreacted propylene from the epoxidation reaction zone for its subsequent recovery and recycle permits a less complicated, lower energy propylene separation. The recycling of spent water from the epoxidation reaction zone and the removal of heavy compounds eliminates a low value water stream and the recovery of heavy hydrocarbons therefrom produces a valuable secondary product.
    • 本发明提供了用于从交替进料流如合成气生产环氧丙烷的综合方法。 在该方法中,由包含氢和碳氧化物的原料流产生环氧丙烷。 将一部分原料流送至含氧化合物生产区以产生包含甲醇和二甲醚的含氧物料流,并将含氧化合物物流送至含有金属磷酸铝催化剂的烯烃生产区以产生丙烯料流。 丙烯流被从由原料流的一部分分离的氢气产生的过氧化氢环氧化。 处理通过环氧化反应产生的废水流以除去重质组分并返回到过氧化氢生产区。 从环氧化反应区返回未反应的丙烯以进行随后的回收和再循环,可以实现较不复杂的较低能量的丙烯分离。 来自环氧化反应区的废水的再循环和重质化合物的去除消除了低价值的水流,并且从其中回收重质烃产生有价值的二次产物。