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
    • 45. 发明申请
    • Systems and Methods for Producing a Crude Product
    • 生产原油产品的系统和方法
    • US20110017635A1
    • 2011-01-27
    • US12506840
    • 2009-07-21
    • Julie ChabotShuwu YangBruce Reynolds
    • Julie ChabotShuwu YangBruce Reynolds
    • C10G65/10C10G47/02C10G65/18
    • C10G47/32C10G47/02C10G47/26C10G65/00C10G65/10C10G65/18
    • A process for hydroprocessing heavy oil feedstock is disclosed. The process operates in once-through mode, employing a plurality of contacting zones and at least a separation zone to convert at least a portion of the heavy oil feedstock to lower boiling hydrocarbons, forming upgraded products. In the once-through upgrade system, little if any of the unconverted material and slurry catalyst mixture is recycled back to the system for further upgrading. The contacting zones operate under hydrocracking conditions, employing a slurry catalyst for upgrading the heavy oil feedstock. The slurry catalyst feed comprises an active metal catalyst having an average particle size of at least 1 micron in a hydrocarbon oil diluent, at a concentration of greater than 500 wppm of active metal catalyst to heavy oil feedstock.
    • 公开了一种加氢处理重油原料的方法。 该方法以一次通过模式运行,采用多个接触区和至少一个分离区,将至少一部分重油原料转化成低沸点烃,形成升级产物。 在一次性升级系统中,很少将未转化的材料和浆料催化剂混合物再循环回系统进行进一步升级。 接触区在加氢裂化条件下运行,使用用于升级重油原料的浆料催化剂。 浆料催化剂进料包含在烃油稀释剂中平均粒度至少为1微米的活性金属催化剂,其浓度大于500wppm的活性金属催化剂与重油原料。
    • 50. 发明申请
    • HYDROPROCESSING CATALYSTS AND METHODS FOR MAKING THEREOF
    • 氢化催化剂及其制备方法
    • US20120004091A1
    • 2012-01-05
    • US13233491
    • 2011-09-15
    • Bo KouJulie Chabot
    • Bo KouJulie Chabot
    • B01J38/48B01J38/60
    • C10G47/02C10G47/26C10G47/32C10G65/00C10G65/10C10G65/18C10G2300/205C10G2300/206C10G2300/701C10G2300/802
    • A method to prepare an improved catalyst feed to a system to upgrade heavy oil. The method comprises: providing a spent catalyst that has been used in a hydroprocessing operation has with a solid content ranging from 5 to 50 wt. % in soluble hydrocarbons and having less than 80% but more than 10% of original catalytic activity; removing at least 50% of the soluble hydrocarbons removed in a deoiling step; treating the deoiled spent catalyst with a treating solution containing at least one of plain water, a mineral acid, an oxidizing agent, and combinations thereof to reduce the concentration of at least one metal contaminant in the deoiled spent catalyst by at least 40%. After treatment, the treated deoiled spent catalyst is slurried in a hydrocarbon medium, and fed to the heavy oil upgrade system as part of the catalyst feed system with a fresh slurry catalyst.
    • 一种制备改进的催化剂进料到系统以升级重油的方法。 该方法包括:提供已经在加氢操作中使用的废催化剂的固体含量范围为5-50wt。 %的可溶性碳氢化合物,并且具有小于80%但大于10%的原始催化活性; 去除在脱油步骤中去除的至少50%的可溶性烃; 用含有浅水,无机酸,氧化剂及其组合中的至少一种的处理溶液处理脱油的废催化剂,以将去除的废催化剂中的至少一种金属污染物的浓度降低至少40%。 处理后,经处理的脱油废催化剂在烃介质中浆化,并作为催化剂进料系统的一部分用新鲜的浆料催化剂进料至重油升级系统。