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    • 1. 发明申请
    • Process for Reducing Fouling From Flash/Separation Apparatus During Cracking of Hydrocarbon Feedstocks
    • 在碳氢化合物原料裂化过程中减少闪蒸/分离装置污垢的方法
    • US20080118416A1
    • 2008-05-22
    • US12019978
    • 2008-01-25
    • Richard StellNicholas Vidonic
    • Richard StellNicholas Vidonic
    • B01J19/26
    • C10G9/00C10G9/20C10G2300/107
    • Hydrocarbon feedstock containing resid is cracked by a process comprising: (a) heating the hydrocarbon feedstock; (b) mixing the heated hydrocarbon feedstock with steam and optionally water to form a mixture stream; (c) introducing the mixture stream to a flash/separation apparatus to form i) a vapor phase at its dew point which partially cracks and loses/or heat causing a temperature decrease and partial condensation of the vapor phase in the absence of added heat to provide coke precursors existing as uncoalesced condensate, and ii) a liquid phase; (d) removing the vapor phase as overhead and the liquid phase as bottoms from the flash/separation apparatus; (e) treating the overhead by contacting with a hydrocarbon-containing nucleating liquid substantially free of resid and comprising components boiling at a temperature of at least about 260° C. (500° F.) under conditions sufficient to at least partially coalesce the coke precursors to provide coke precursor liquid, in the form of hydrocarbon droplets or a continuous hydrocarbon liquid phase; (f) collecting and removing the droplets; (g) directing the treated overhead from which the droplets are removed, to a heater to provide a heated vapor phase; (h) cracking the heated vapor phase in a radiant section of a pyrolysis furnace to produce an effluent comprising olefins, the pyrolysis furnace comprising a radiant section and a convection section; and (i) quenching the effluent and recovering cracked product therefrom. An apparatus for carrying out the process is also provided.
    • 含有渣油的烃原料通过包括以下步骤的方法裂化:(a)加热烃原料; (b)将加热的烃原料与蒸汽和任选的水混合以形成混合物流; (c)将混合物流引入闪蒸/分离装置以形成i)其露点处的气相,其在不存在加热的情况下部分地裂开和损失/或加热导致气相的温度降低和部分冷凝, 提供作为未聚结的冷凝物存在的焦炭前体,和ii)液相; (d)从闪蒸/分离装置中除去气相作为塔顶馏出物和液相作为底部物质; (e)通过与基本上不含渣油的含烃成核液体接触来处理塔顶馏出物,并且包括在足以使焦炭至少部分聚结的条件下在至少约260℃(500°F)的温度下沸腾的组分 以烃液滴或连续烃液相的形式提供焦炭前体液体的前体; (f)收集和去除液滴; (g)将经除去的液滴处理的塔顶导向加热器以提供加热的气相; (h)在热解炉的辐射段中裂解加热的气相以产生包含烯烃的流出物,所述热解炉包括辐射段和对流段; 和(i)淬灭流出物并从其中回收裂化产物。 还提供了一种用于执行该过程的装置。
    • 3. 发明申请
    • Outlet fitting for double pipe quench exchanger
    • 双管淬火换热器出口配件
    • US20070193729A1
    • 2007-08-23
    • US11356475
    • 2006-02-17
    • Dave SpicerNicholas Vidonic
    • Dave SpicerNicholas Vidonic
    • C10G9/00F28F19/00
    • F28D7/106B01J19/0013B01J19/2415C10G9/002F16L39/005F28D2021/0075F28F9/0246
    • A novel outlet fitting for use in connection with a heat exchanger. The heat exchanger is used in the role of a quench exchanger for cooling cracking effluent and solves particular problems associated with gas-oil cracking applications and other heavy feed based applications wherein differences between process outlet temperature and coolant temperatures are larger than in, for example, naphtha and gas cracking applications. The specific solution is achieved through a novel outlet fitting for the quench exchanger that eliminates the need for a steam purge, addresses thermal stress issues and reduces pressure drop within the system. The outlet fitting includes internal insulation to avoid the need for a steam purge. In addition, the outlet fitting includes a low-angle diffuser with an angle of less than 7 degrees and preferably less than 5 degrees.
    • 一种用于与热交换器连接使用的新型出口接头。 热交换器用于冷却裂解流出物的淬火换热器,并且解决与瓦斯油裂解应用和其它基于重的进料的应用相关的特定问题,其中工艺出口温度和冷却剂温度之间的差异大于例如, 石脑油和气体裂解应用。 具体的解决方案是通过一个用于淬火换热器的新型出口配件来实现的,它不需要蒸汽吹扫,解决热应力问题并减少系统内的压降。 出口配件包括内部绝缘,以避免蒸汽吹扫的需要。 此外,出口配件包括具有小于7度,优选小于5度的角度的低角度扩散器。
    • 5. 发明申请
    • Process for reducing fouling from flash/separation apparatus during cracking of hydrocarbon feedstocks
    • 用于在烃原料开裂期间减少闪蒸/分离装置的结垢的方法
    • US20060014993A1
    • 2006-01-19
    • US10891981
    • 2004-07-14
    • Richard StellNicholas Vidonic
    • Richard StellNicholas Vidonic
    • C07C4/04C10G9/14
    • C10G9/20C10G9/00
    • Hydrocarbon feedstock containing resid is cracked by a process comprising: (a) heating said hydrocarbon feedstock; (b) mixing the heated hydrocarbon feedstock with steam to form a mixture stream; (c) introducing the mixture stream to a flash/separation apparatus to form i) a vapor phase comprising coke precursors existing as uncoalesced condensate, and ii) a liquid phase; (d) removing the vapor phase as overhead and the liquid phase as bottoms from the flash/separation apparatus; (e) treating the overhead by contacting with a condensing means downstream of the flash/separation apparatus to at least partially coalesce the coke precursors to provide residue hydrocarbon liquid, and subsequently removing the hydrocarbon liquid; (f) heating the treated overhead to provide a heated vapor phase (g) cracking the heated vapor phase in a radiant section of a pyrolysis furnace to produce an effluent comprising olefins, the pyrolysis furnace comprising a radiant section and a convection section; and (h) quenching the effluent and recovering cracked product therefrom. An apparatus for carrying out the process is also provided.
    • 含有渣油的烃原料通过包括以下步骤的方法裂化:(a)加热所述烃原料; (b)将加热的烃原料与蒸汽混合以形成混合物流; (c)将混合物流引入闪蒸/分离装置以形成i)包含作为未经缩聚的冷凝物存在的焦炭前体的气相,和ii)液相; (d)从闪蒸/分离装置中除去气相作为塔顶馏出物和液相作为底部物质; (e)通过与闪蒸/分离装置下游的冷凝装置接触来处理塔顶馏出物,以至少部分地将焦炭前体聚结以提供残余烃液体,随后除去烃液体; (f)加热经处理的塔顶馏出物以提供加热的气相(g)在热解炉的辐射段中裂化加热的气相以产生包含烯烃的流出物,所述热解炉包括辐射段和对流段; 和(h)淬灭流出物并从其中回收裂化产物。 还提供了一种用于执行该过程的装置。
    • 6. 发明申请
    • Process for reducing fouling from flash/separation apparatus during cracking of hydrocarbon feedstocks
    • 用于在烃原料开裂期间减少闪蒸/分离装置的结垢的方法
    • US20060014992A1
    • 2006-01-19
    • US10891795
    • 2004-07-14
    • Richard StellNicholas Vidonic
    • Richard StellNicholas Vidonic
    • C07C4/04C10G9/14
    • C10G9/00C10G9/20C10G2300/107
    • Hydrocarbon feedstock containing resid is cracked by a process comprising: (a) heating the hydrocarbon feedstock; (b) mixing the heated hydrocarbon feedstock with steam and optionally water to form a mixture stream; (c) introducing the mixture stream to a flash/separation apparatus to form i) a vapor phase at its dew point which partially cracks and loses/or heat causing a temperature decrease and partial condensation of the vapor phase in the absence of added heat to provide coke precursors existing as uncoalesced condensate, and ii) a liquid phase; (d) removing the vapor phase as overhead and the liquid phase as bottoms from the flash/separation apparatus; (e) treating the overhead by contacting with a hydrocarbon-containing nucleating liquid substantially free of resid and comprising components boiling at a temperature of at least about 260° C. (500° F.) under conditions sufficient to at least partially coalesce the coke precursors to provide coke precursor liquid, in the form of hydrocarbon droplets or a continuous hydrocarbon liquid phase; (f) collecting and removing the droplets; (g) directing the treated overhead from which the droplets are removed, to a heater to provide a heated vapor phase; (h) cracking the heated vapor phase in a radiant section of a pyrolysis furnace to produce an effluent comprising olefins, the pyrolysis furnace comprising a radiant section and a convection section; and (i) quenching the effluent and recovering cracked product therefrom. An apparatus for carrying out the process is also provided.
    • 含有渣油的烃原料通过包括以下步骤的方法裂化:(a)加热烃原料; (b)将加热的烃原料与蒸汽和任选的水混合以形成混合物流; (c)将混合物流引入闪蒸/分离装置以形成i)其露点处的气相,其在不存在加热的情况下部分地裂开和损失/或加热导致气相的温度降低和部分冷凝, 提供作为未聚结的冷凝物存在的焦炭前体,和ii)液相; (d)从闪蒸/分离装置中除去气相作为塔顶馏出物和液相作为底部物质; (e)通过与基本上不含渣油的含烃成核液体接触来处理塔顶馏出物,并且包括在足以使焦炭至少部分聚结的条件下在至少约260℃(500°F)的温度下沸腾的组分 以烃液滴或连续烃液相的形式提供焦炭前体液体的前体; (f)收集和去除液滴; (g)将经除去的液滴处理的塔顶导向加热器以提供加热的气相; (h)在热解炉的辐射段中裂解加热的气相以产生包含烯烃的流出物,所述热解炉包括辐射段和对流段; 和(i)淬灭流出物并从其中回收裂化产物。 还提供了一种用于执行该过程的装置。