利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

6 条记录 (耗时 0.012 秒)

    PROCESS FOR PRODUCING HYDROCARBON OIL
    2.
    发明公开
    PROCESS FOR PRODUCING HYDROCARBON OIL 审中-公开
    生产烃油的方法

    公开(公告)号：EP2351816A1

    公开(公告)日：2011-08-03

    申请号：EP09814597.2

    申请日：2009-09-16

    申请人： JX Nippon Oil & Energy Corporation

    发明人： IGUCHI, Yasutoshi ,  HAMAMATSU, Tatsuo ,  ONO, Hideki ,  KOYAMA, Akira ,  IKI, Hideshi

    IPC分类号： C10G3/00 ,  C10G45/58 ,  C10G45/62 ,  C10G69/02

    CPC分类号： C10G3/46 ,  C10G3/49 ,  C10G3/50 ,  C10G45/04 ,  C10G45/06 ,  C10G45/08 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/202 ,  C10G2300/207 ,  C10G2300/4006 ,  C10G2300/4012 ,  C10G2300/4081 ,  C10G2300/70 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  Y02P30/20

    摘要： The method for manufacturing a hydrocarbon oil of the present invention comprises a first step wherein a plurality of reaction zones filled with a specific catalyst is disposed in series and a feedstock oil containing an oxygen-containing hydrocarbon compound derived from an animal or vegetable oil is supplied and hydrotreated under the conditions of a hydrogen pressure of 1 MPa or more and 10 MPa or less in each of the reaction zones; and a second step wherein hydrogen, hydrogen sulfide, carbon dioxide and water are removed from a product to be treated obtained in the first step to obtain a hydrocarbon oil. Among the plurality of reaction zones, the inlet temperature of the reaction zone disposed on the most upstream side is 150°C or more and 250°C or less, the inlet temperature of the second most upstream reaction zone or below is equal to or higher than the condensation temperature of water, and the outlet temperature of the reaction zone disposed on the most downstream side is 260°C or more and 360°C or less. The feedstock oil comprises a recycled oil containing a specific amount of a part of the hydrocarbon oil obtained in the second step and a specific amount of a sulfur-containing hydrocarbon compound.

    摘要翻译： 本发明的烃油的制造方法包括：将填充有特定催化剂的多个反应区串联配置，供给含有来源于动植物油的含氧烃化合物的原料油的第一工序 并在每个反应区中在1MPa以上且10MPa以下的氢气压力的条件下进行加氢处理; 和第二步骤，其中从第一步骤中获得的待处理产物中除去氢气，硫化氢，二氧化碳和水以获得烃油。 在多个反应区中，位于最上游侧的反应区的入口温度为150℃以上且250℃以下，第二最上游反应区的入口温度以下等于或高于 比水的冷凝温度低，位于最下游侧的反应区的出口温度为260℃以上且360℃以下。 原料油包含含有特定量的第二步得到的一部分烃油和特定量的含硫烃化合物的循环油。

    FLUID CATALYTIC CRACKING PROCESS FOR HEAVY OIL
    4.
    发明公开
    FLUID CATALYTIC CRACKING PROCESS FOR HEAVY OIL 审中-公开
    FLUIDKATALYTISCHES KRACKVERFAHRENFÜRSCHWERÖL

    公开(公告)号：EP3098287A1

    公开(公告)日：2016-11-30

    申请号：EP15740687.7

    申请日：2015-01-20

    申请人： JX Nippon Oil & Energy Corporation

    发明人： ONO, Hideki ,  OHUCHI, Tai ,  IWAMA, Marie ,  ISHIZUKA, Tatsushi

    IPC分类号： C10G11/05 ,  C10G11/18

    CPC分类号： C10G11/05 ,  C10G11/18 ,  C10G2300/1033 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2400/20

    摘要： Provided is a process for fluid catalytic cracking of a heavy oil by contacting the oil with a catalyst at an elevated temperature for a short period of time to produce light olefins such as propylene and butene. The process comprises contacting the heavy oil with a catalyst comprising as a constituent thereof a fluid catalytic cracking catalyst with a weight ratio (Wmat/Wusy) of an active matrix weight (Wmat) to an ultrastable Y type zeolite weight (Wusy) of 0 to 0.3, under conditions where the reaction zone outlet temperature is from 580 to 630°C, the catalyst/oil ratio is from 15 to 40 weight/weight and the residence time of hydrocarbon in the reaction zone is from 0.1 to 1.0 second.

    摘要翻译： 提供了一种通过使油与催化剂在高温下短时间接触以产生轻质烯烃如丙烯和丁烯的流化催化裂化重油的方法。 该方法包括使重油与包含作为其组分的催化剂接触，其具有活性基质重量（Wmat）的重量比（Wmat / Wusy）至0至超稳定Y型沸石重量（Wusy）为0的流化催化裂化催化剂 0.3，在反应区出口温度为580〜630℃的条件下，催化剂/油比为15〜40重量/重量，烃在反应区中的停留时间为0.1〜1.0秒。

    PROCESS FOR PRODUCING HYDROCARBON OIL
    6.
    发明公开
    PROCESS FOR PRODUCING HYDROCARBON OIL 审中-公开
    VERFAHREN ZUR HERSTELLUNG VONKOHLENWASSERSTOFFÖL

    公开(公告)号：EP2333030A1

    公开(公告)日：2011-06-15

    申请号：EP09814593.1

    申请日：2009-09-16

    申请人： JX Nippon Oil & Energy Corporation

    发明人： HAMAMATSU, Tatsuo ,  ONO, Hideki ,  IGUCHI, Yasutoshi ,  IKI, Hideshi ,  KINOSHITA, Yoshihiko

    IPC分类号： C10G67/10 ,  C10G3/00 ,  C10G19/00 ,  C10G45/04

    CPC分类号： C10G45/02 ,  C10G3/46 ,  C10G3/49 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/202 ,  C10G2300/4018 ,  Y02P30/20

    摘要： A method for manufacturing a hydrocarbon oil, comprising: a first step wherein a feedstock oil containing an oxygen-containing organic compound and a water-insoluble chlorine-containing compound is brought into contact with a hydrogenation catalyst comprising a support containing a porous inorganic oxide and one or more metals selected from Group VIA and Group VIII of the periodic table supported on the support in the presence of hydrogen to generate a hydrocarbon oil and water in a vapor state by the hydrodeoxygenation of an oxygen-containing organic compound and convert the water-insoluble chlorine-containing compound into a water-soluble chlorine-containing compound; a second step wherein the water in the reaction product of the first step is maintained in a vapor state and the reaction product of the first step is brought into contact with a nitrogen-containing Brønsted base compound which has a boiling point at normal pressure of 100°C or less and is water-soluble to obtain a product to be treated; and a third step wherein the product to be treated is cooled to a temperature not higher than the temperature at which water in a vapor state is liquefied to form an aqueous phase containing a water-soluble chlorine-containing compound and a nitrogen-containing Bronsted base compound and then separate the aqueous phase from an oil to be treated to obtain a product oil containing a hydrocarbon oil.

    摘要翻译： 一种烃油的制造方法，包括：第一工序，其中含有含氧有机化合物的原料油和不溶于水的含氯化合物与包含含有多孔无机氧化物的载体的氢化催化剂接触， 选自元素周期表第VIA族和第VIII族的一种或多种金属在氢气存在下负载在载体上以通过含氧有机化合物的加氢脱氧产生烃油和蒸气状态的水， 不溶性含氯化合物变成水溶性含氯化合物; 第二步骤，其中第一步骤的反应产物中的水保持蒸气状态，并使第一步的反应产物与常压下的沸点为100的含氮布朗斯台德碱化合物接触 ℃以下，为水溶性，得到待处理品; 以及第三步骤，其中待处理的产品被冷却至不高于蒸汽状态的水液化的温度的温度，以形成含有水溶性含氯化合物和含氮Bronsted碱的水相 然后将水相与待处理的油分离，得到含有烃油的产物油。