METHOD FOR OPTIMIZING THE OPERATION OF A HYDROCARBON SYNTHESIS UNIT STARTING FROM SYNTHESIS GAS, BY CONTROLLING THE PARTIAL PRESSURE OF CO
    1.
    发明申请
    METHOD FOR OPTIMIZING THE OPERATION OF A HYDROCARBON SYNTHESIS UNIT STARTING FROM SYNTHESIS GAS, BY CONTROLLING THE PARTIAL PRESSURE OF CO 有权
    通过控制CO的部分压力来优化从合成气开始的烃合成装置的运行的方法

    公开(公告)号:US20120129961A1

    公开(公告)日:2012-05-24

    申请号:US13377193

    申请日:2010-05-18

    IPC分类号: C07C1/04

    摘要: A method is described for optimizing the operation of a reaction section for the synthesis of hydrocarbons from a feed comprising synthesis gas, operated in the presence of a catalyst comprising cobalt, said method comprising the following steps: a) determining the theoretical partial pressure of CO in the reaction section; b) optionally, adjusting the partial pressure of CO determined in step a) to a value of 4 bar or higher; c) determining a new value for the theoretical partial pressure of CO in the reaction section.

    摘要翻译: 描述了一种用于优化用于从包含合成气的原料合成烃的反应段的操作的方法,所述合成气在包含钴的催化剂存在下操作,所述方法包括以下步骤:a)确定CO的理论分压 在反应部分; b)任选地,将步骤a)中测定的CO的分压调节至4巴或更高的值; c)确定反应段中CO的理论分压的新值。

    Method for optimizing the operation of a hydrocarbon synthesis unit starting from synthesis gas, by controlling the partial pressure of CO
    2.
    发明授权
    Method for optimizing the operation of a hydrocarbon synthesis unit starting from synthesis gas, by controlling the partial pressure of CO 有权
    通过控制CO的分压来优化从合成气开始的烃合成单元的操作的方法

    公开(公告)号:US08940802B2

    公开(公告)日:2015-01-27

    申请号:US13377193

    申请日:2010-05-18

    IPC分类号: C07C1/04 C10G2/00 B01J23/75

    摘要: A method is described for optimizing the operation of a reaction section for the synthesis of hydrocarbons from a feed comprising synthesis gas, operated in the presence of a catalyst comprising cobalt, said method comprising the following steps: a) determining the theoretical partial pressure of CO in the reaction section; b) optionally, adjusting the partial pressure of CO determined in step a) to a value of 4 bar or higher; c) determining a new value for the theoretical partial pressure of CO in the reaction section.

    摘要翻译: 描述了一种用于优化用于从包含合成气的原料合成烃的反应段的操作的方法,所述合成气在包含钴的催化剂存在下操作,所述方法包括以下步骤:a)确定CO的理论分压 在反应部分; b)任选地,将步骤a)中测定的CO的分压调节至4巴或更高的值; c)确定反应段中CO的理论分压的新值。

    Process for recovering metals from a stream rich in hydrocarbons and carbonaceous residues
    5.
    发明授权
    Process for recovering metals from a stream rich in hydrocarbons and carbonaceous residues 有权
    从富含烃和碳质残渣的物流中回收金属的方法

    公开(公告)号:US08440152B2

    公开(公告)日:2013-05-14

    申请号:US13377036

    申请日:2010-06-01

    IPC分类号: C22B3/00

    摘要: A process for recovering metals from a stream rich in hydrocarbons and carbonaceous residues by means of a treatment section, characterized in that it comprises the following steps: sending said stream to a primary treatment, effected in one or more steps, wherein said stream is treated in the presence of a fluxant agent in a suitable apparatus, at a temperature ranging from 80 to 180° C., preferably from 100 to 160° C., and subjected to liquid/solid separation in order to obtain a clarified product essentially consisting of liquids and a cake (oilcake); possibly subjecting the separated cake to drying, in order to remove the hydrocarbon component having a boiling point lower than a temperature ranging from 300 to 350° C. from the cake; sending the cake, possibly dried, to a secondary thermal treatment comprising: a flameless pyrolysis of the cake effected between 400 and 800° C., preferably between 500 and 670° C.; an oxidation of the pyrolysis residue effected in an oxidizing environment and at temperatures ranging from 400 to 800° C., preferably from 500 to 700° C.

    摘要翻译: 一种通过处理部分从富含烃和碳质残余物的物流中回收金属的方法,其特征在于其包括以下步骤:将一个或多个步骤中的所述物流送入初级处理,其中所述物流被处理 在合适的装置中,在80至180℃,优选100至160℃的温度下,在助流剂存在下进行液/固分离,以获得基本上由 液体和蛋糕(油饼); 可能使分离的饼干经历干燥,以便从饼中除去沸点低于300-350℃的沸点的烃成分; 将可能干燥的蛋糕送到二次热处理中,其包括:在400和800℃之间,优选在500和670℃之间进行无蛋白质的热解。 在氧化环境中和在400至800℃,优选500至700℃的温度下进行热解残留物的氧化。

    PROCESS FOR RECOVERING METALS FROM A STREAM RICH IN HYDROCARBONS AND CARBONACEOUS RESIDUES
    6.
    发明申请
    PROCESS FOR RECOVERING METALS FROM A STREAM RICH IN HYDROCARBONS AND CARBONACEOUS RESIDUES 有权
    从碳氢化合物和碳氢化合物中回收金属的方法

    公开(公告)号:US20120134899A1

    公开(公告)日:2012-05-31

    申请号:US13377036

    申请日:2010-06-01

    IPC分类号: C01G1/02

    摘要: A process for recovering metals from a stream rich in hydrocarbons and carbonaceous residues by means of a treatment section, characterized in that it comprises the following steps: sending said stream to a primary treatment, effected in one or more steps, wherein said stream is treated in the presence of a fluxant agent in a suitable apparatus, at a temperature ranging from 80 to 180° C., preferably from 100 to 160° C., and subjected to liquid/solid separation in order to obtain a clarified product essentially consisting of liquids and a cake (oilcake); possibly subjecting the separated cake to drying, in order to remove the hydrocarbon component having a boiling point lower than a temperature ranging from 300 to 350° C. from the cake; sending the cake, possibly dried, to a secondary thermal treatment comprising: a flameless pyrolysis of the cake effected between 400 and 800° C., preferably between 500 and 670° C.; an oxidation of the pyrolysis residue effected in an oxidizing environment and at temperatures ranging from 400 to 800° C., preferably from 500 to 700° C.

    摘要翻译: 一种通过处理部分从富含烃和碳质残余物的物流中回收金属的方法,其特征在于其包括以下步骤:将所述物流送入初级处理,一个或多个步骤进行,其中所述物流被处理 在合适的装置中,在80至180℃,优选100至160℃的温度下,在助流剂存在下进行液/固分离,以获得基本上由 液体和蛋糕(油饼); 可能使分离的饼干经历干燥,以便从饼中除去沸点低于300-350℃的沸点的烃成分; 将可能干燥的蛋糕送到二次热处理中,其包括:在400和800℃之间,优选在500和670℃之间进行无蛋白质的热解。 在氧化环境中和在400至800℃,优选500至700℃的温度下进行热解残留物的氧化。

    Process for producing mixtures of methanol and higher alcohols
    7.
    发明授权
    Process for producing mixtures of methanol and higher alcohols 失效
    制备甲醇和高级醇混合物的方法

    公开(公告)号:US5767166A

    公开(公告)日:1998-06-16

    申请号:US732597

    申请日:1996-10-15

    IPC分类号: C07C29/153 C10L1/02 C07C1/04

    CPC分类号: C07C29/153 C10L1/02

    摘要: Process for producing mixtures of methanol and higher alcohols comprising feeding, into the reaction zone equipped with a catalytic system, H.sub.2, CO and possibly inert products with a molar ratio H.sub.2 /CO of between 0.2 and 10, at a temperature of between 200.degree. and 460.degree. C., at a pressure of between 2,000 and 30,000 KPa, and at a space velocity of between 1,000 and 40,000 GHSV, wherein the catalytic system corresponds to the following empirical formula: Zn.sub.x Cr.sub.y O.sub.t +z%M.sub.2 O wherein the x/y ratio is greater than 0.5 and less than 1, t is what is necessary for satisfying the valence with which the various elements appear in the catalyst, M is an alkaline metal selected from potassium and cesium, z, representing the percentage of alkaline oxide of the final catalyst, when the metal is potassium, is between 0.01 and 8 and, when the metal is cesium, between 0.01 and 20.6.

    摘要翻译: 制备甲醇和高级醇的混合物的方法,包括在装有催化体系的反应区中,在H 2 / CO和H 2 / CO摩尔比为0.2至10之间的温度下,在200°和 460℃,压力为2,000至30,000KPa,空间速度为1,000至40,000 GHSV,其中催化体系对应于以下经验式:Zn x CryOt + z%M 2 O其中x / y比为 大于0.5且小于1,t是满足各种元素在催化剂中出现的化合价所必需的,M是选自钾和铯的碱金属,z代表最终催化剂的碱性氧化物的百分比 当金属为钾时,为0.01〜8,当金属为铯时,为0.01〜20.6。

    Process for the skeleton isomerization of linear olefins
    8.
    发明授权
    Process for the skeleton isomerization of linear olefins 失效
    线性烯烃骨架异构化方法

    公开(公告)号:US5600054A

    公开(公告)日:1997-02-04

    申请号:US381062

    申请日:1995-01-31

    IPC分类号: B01J21/02 C07C5/27

    CPC分类号: B01J21/02 C07C5/277

    摘要: Process for the skeleton isomerization of linear olefins, preferably n-butenes or n-pentenes, which consists in putting said olefins in contact with a catalyst comprising alumina on whose surface boron oxide is deposited in a quantity which is lower than 2.1.times.10.sup.-4 g/m.sup.2 of the surface of the alumina.

    摘要翻译: 线性烯烃,优选正丁烯或正戊烯骨架异构化的方法,其包括将所述烯烃与包含氧化铝的催化剂接触,所述催化剂在其表面上沉积氧化硼,其量低于2.1×10 -4 g / m2的氧化铝表面。