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    • 1. 发明授权
    • Process for the production of pure neohexanol
    • 生产纯新己醇的方法
    • US4433175A
    • 1984-02-21
    • US444265
    • 1982-11-24
    • Manfred Kaufhold
    • Manfred Kaufhold
    • C07C29/136B01J23/00C07B61/00C07C27/00C07C29/149C07C31/125C07C45/00C07C51/44C07C67/00
    • C07C45/002C07C29/149C07C51/44C07C67/08C07C67/54
    • For the production of neohexanol with a purity above 99%, a chlorine content of less than 10 ppm, and a sulfur content of less than 5 ppm, 3,3-dimethylbutyric acid with a chlorine content below 650 ppm, preferably below 100 ppm, is first esterified, optionally after distillatory separation into a portion richer in chlorine with a chlorine content above 650 ppm, preferably above 100 ppm, and into a portion low in chlorine with a chlorine content below 650 ppm, preferably below 100, with an alcohol boiling above 117.degree. C., preferably an octyl alcohol. The resultant ester is separated by distillation into fractions richer in chlorine with chlorine contents above 10 ppm and into fractions low in chlorine with chlorine contents below 10 ppm. The ester of low chlorine contents below 10 ppm is hydrogenated to neohexanol over a barium-activated copper chromite catalyst under a pressure of 200-300 bar, at 120.degree.-22.degree. C., and with catalyst loads of 0.05-1.0 liter of hydrogenation feed/liter of catalyst . hour. The high purity of the neohexanol permits catalytic dehydrogenation to neohexanal.
    • 为了生产纯度高于99%,氯含量小于10ppm,硫含量小于5ppm的新己醇,氯含量低于650ppm的3,3-二甲基丁酸,优选低于100ppm, 首先被酯化,任选地在蒸馏分离成氯含量高于650ppm,优选高于100ppm的部分中的部分中,并且进入氯含量低于650ppm,优选低于100的部分低于醇的沸点 117℃以上,优选为辛醇。 通过蒸馏将所得的酯分离成富含氯,氯含量高于10ppm的馏分,氯含量低于10ppm的氯含量。 低于10ppm的低氯含量的酯在200-300巴的压力下,在120℃-22℃,催化剂负载为0.05-1.0升的氢化催化剂上,在钡活化的亚铬酸铜催化剂上氢化成新己醇 进料/升催化剂。 小时。 新己醇的高纯度允许催化脱氢至新己醛。
    • 3. 发明授权
    • Process for extracting extensively emulsion-free oil from a subterranean
reservoir
    • 从地下储层中大量提取无乳油的方法
    • US4542790A
    • 1985-09-24
    • US633680
    • 1984-07-25
    • Dieter Balzer
    • Dieter Balzer
    • C09K8/584E21B43/22
    • C09K8/584Y10S507/936
    • A process for extracting extensively emulsion-free oil from a subterranean deposit, the formation water of which has a medium or high total salinity and has a relatively low alkaline earth metal ion concentration, comprising injecting into an injection well therein a 1-20% strength aqueous tenside solution or dispersion in formation water of a mixture of 10-90% of carboxymethylated ethoxylates of the formulaR--(OCH.sub.2 CH.sub.2).sub.n --OCH.sub.2 --COOMand 90-10% of ethoxylates of the formulaR--(OCH.sub.2 CH.sub.2).sub.n --OH,whereinR is a linear or branched hydrocarbon aliphatic group of 4-20 carbon atoms or an alkylphenyl group of 1-14 carbon atoms in the alkyl group,n is 3-15, andM is an alkali or alkaline earth metal ion or ammonium, wherein alkaline earth metal ions are contained in the tenside solution or dispersion in such a concentration that the phase inversion temperature of the system:crude oil/formation water/tenside solution or dispersion, lies at most 10.degree. C. above the deposit temperature.
    • 一种从地下沉积物中提取广泛无乳液的油的方法,其地层水具有中等或高总盐度并具有相对较低的碱土金属离子浓度,包括向注入井注入1-20%的强度 10-90%的式R-(OCH 2 CH 2)n -OCH 2 -COOM的羧甲基化乙氧基化物和90-10%式R-(OCH 2 CH 2)n -OH的乙氧基化物的混合物的地层水中的水性表面活性剂溶液或分散体 其中R为4-20个碳原子的直链或支链烃脂族基或烷基中1-14个碳原子的烷基苯基,n为3-15,M为碱金属或碱土金属离子或铵 其中碱土金属离子包含在表面活性剂溶液或分散体中,其浓度使得原油/地层水/表面活性剂溶液或分散体系的相转变温度高于沉积温度10℃以上。
    • 4. 发明授权
    • Process for oil recovery from a subterranean reservoir
    • 从地下油藏采油的工艺
    • US4485873A
    • 1984-12-04
    • US413908
    • 1982-09-01
    • Dieter BalzerKurt Kosswig
    • Dieter BalzerKurt Kosswig
    • C09K8/584E21B43/22
    • C09K8/584Y10S507/936
    • A process for the recovery of extensively emulsion-free oil from a subterranean reservoir of medium or high salinity comprises forcing into an injection well a 0.1-20% (e.g., 1-20%) by weight solution or dispersion in formation water of carboxymethylated ethoxylates of the formulaR--(OCH.sub.2 CH.sub.2).sub.n --OCH.sub.2 --COOM,whereinR is a linear or branched aliphatic residue of 4-20 carbon atoms or an alkylaromatic or dialkylaromatic residue of 1-14 carbon atoms in the alkyl group,n is 1-30, e.g., 3-30, andM is an alkali or alkaline earth metal ion or ammonium,and the degree of carboxymethylation is between 10 and 100%, wherein the carboxymethylated oxethylate is selected so that the phase inversion temperature of the system: crude oil/formation water/tenside/optional additives, is 0.degree.-10.degree. C. above the reservoir temperature.
    • 从中等或高盐度的地下储层回收广泛不含乳液的油的方法包括强制进入注入井,其重量为羧甲基化乙氧基化物地层水中的0.1-20%(例如1-20%)溶液或分散体 其中R是4-20个碳原子的直链或支链脂肪族残基或烷基中1-14个碳原子的烷基芳基或二烷基芳基残基,n是1-(2-氯苯基) 30,例如3-30,M是碱金属或碱土金属离子或铵,羧甲基化度在10〜100%之间,其中选择羧甲基化的氧乙酸酯,使得体系的相转化温度:粗 油/地层水/表面活性剂/任选添加剂,高于储层温度0℃-10℃。
    • 8. 发明授权
    • High-molecular weight linear polyesters and a process for preparing them
    • 高分子线性聚酯及其制备方法
    • US4328059A
    • 1982-05-04
    • US195538
    • 1980-10-09
    • Gernot HorlbeckKlaus Burzin
    • Gernot HorlbeckKlaus Burzin
    • C08G63/183C09D167/02C09J167/02B05D3/00C08K3/22C08L67/02C09J3/16
    • C09D167/02C08G63/183C08K3/32C08K5/52C09J167/02
    • High molecular weight linear polyesters advantageous for use as hot melt adhesives and powder coating agents, are prepared by a process for preparing a high-molecular weight, linear copolyester by condensing 40-85 molar percent of terephthalic acid optionally in the form of a dialkyl ester, half of which component can optionally be replaced by another dicarboxylic acid also optionally in the dialkyl ester form, and 60-15 molar percent of adipic acid, with an alkanediol of 2-6 carbon atoms in its carbon chain, at an elevated temperature in the presence of a conventional catalyst, in a first condenstation stage which is an interesterification or esterification stage and a second condenstation stage which is a polycondensation stage, whereby a copolyester melt is produce. The process comprises, before or during the first condensation stage, adding 0.005-01 molar percent, based on the total acid component, of a C.sub.6 - aryl or C.sub.7 - alkaryl ester of phosphorous acid or of phosphoric acid to the reaction mixture; and, after termination of the second condensation stage, adding 0.01-0.2 molar percent, based on the total acid component, of hypophosphorous acid to the finished copolyester melt.
    • 优选用作热熔粘合剂和粉末涂料的高分子量线性聚酯通过一种制备高分子量线性共聚酯的方法制备,该方法通过将40-85摩尔%的对苯二甲酸任选以二烷基酯的形式 其中一半的组分可以任选地被二烷基酯形式的另外的二羧酸和在其碳链中具有2-6个碳原子的链烷二醇的60-15摩尔%的己二酸在升高的温度 在作为酯交换阶段的第一冷凝阶段和作为缩聚阶段的第二冷凝阶段中常规催化剂的存在,由此产生共聚酯熔体。 该方法包括在第一缩合阶段之前或期间,向反应混合物中加入0.005-1摩尔%的基于总酸成分的亚磷酸或磷酸的C 6 - 芳基或C 7 - 烷芳基酯; 并且在第二冷凝阶段终止后,向成品共聚酯熔体中加入基于总酸成分的0.01-0.2摩尔%的次磷酸。