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    • 2. 发明授权
    • Process and draft control system for use in cracking a heavy hydrocarbon feedstock in a pyrolysis furnace
    • 用于裂解热解炉中重质烃原料的工艺和牵伸控制系统
    • US07351872B2
    • 2008-04-01
    • US10851495
    • 2004-05-21
    • Richard C. StellSubramanian AnnamalaiJames M. Frye
    • Richard C. StellSubramanian AnnamalaiJames M. Frye
    • C07C4/02C10G9/36
    • C10G9/00C10G9/20C10G9/206
    • A process and control system for cracking a heavy hydrocarbon feedstock containing non-volatile hydrocarbons comprising heating the heavy hydrocarbon feedstock, mixing the heated heavy hydrocarbon feedstock with a dilution steam stream to form a mixture stream having a vapor phase and a liquid phase, separating the vapor phase from the liquid phase in a separation vessel, and cracking the vapor phase in the furnace, wherein the furnace draft is continuously measured and periodically adjusted to control the temperature of the stream entering the vapor/liquid separator and thus controlling the ratio of vapor to liquid separated in the separation vessel; and wherein in a preferred embodiment the means for adjusting the draft comprises varying the speed of at least one furnace fan, possibly in combination with adjusting the position of the furnace fan damper(s) or the furnace burner dampers(s).
    • 一种用于裂化含有非挥发性烃的重质烃原料的方法和控制系统,包括加热重质烃原料,将加热的重质烃原料与稀释蒸汽流混合以形成具有气相和液相的混合物流,将 在分离容器中的液相的气相,并且在炉中裂化气相,其中连续测量并周期性地调节炉汲取气,以控制进入蒸汽/液体分离器的流的温度,从而控制蒸汽/ 在分离容器中分离液体; 并且其中在优选实施例中,用于调节通风的装置包括改变至少一个炉风扇的速度,可能与调节炉风扇风门或炉燃烧器风门的位置相结合。
    • 7. 发明授权
    • Process and draft control system for use in cracking a heavy hydrocarbon feedstock in a pyrolysis furnace
    • 用于裂解热解炉中重质烃原料的工艺和牵伸控制系统
    • US07544852B2
    • 2009-06-09
    • US12020000
    • 2008-01-25
    • Richard C. StellSubramanian AnnamalaiJames M. Frye
    • Richard C. StellSubramanian AnnamalaiJames M. Frye
    • C07C4/02C10G9/36
    • C10G9/00C10G9/20C10G9/206
    • A process and control system for cracking a heavy hydrocarbon feedstock containing non-volatile hydrocarbons comprising heating the heavy hydrocarbon feedstock, mixing the heated heavy hydrocarbon feedstock with a dilution steam stream to form a mixture stream having a vapor phase and a liquid phase, separating the vapor phase from the liquid phase in a separation vessel, and cracking the vapor phase in the furnace, wherein the furnace draft is continuously measured and periodically adjusted to control the temperature of the stream entering the vapor/liquid separator and thus controlling the ratio of vapor to liquid separated in the separation vessel; and wherein in a preferred embodiment the means for adjusting the draft comprises varying the speed of at least one furnace fan, possibly in combination with adjusting the position of the furnace fan damper(s) or the furnace burner dampers(s).
    • 一种用于裂化含有非挥发性烃的重质烃原料的方法和控制系统,包括加热重质烃原料,将加热的重质烃原料与稀释蒸汽流混合以形成具有气相和液相的混合物流,将 在分离容器中的液相的气相,并且在炉中裂化气相,其中连续测量并周期性地调节炉汲取气,以控制进入蒸汽/液体分离器的流的温度,从而控制蒸汽/ 在分离容器中分离液体; 并且其中在优选实施例中,用于调节通风的装置包括改变至少一个炉风扇的速度,可能与调节炉风扇风门或炉燃烧器风门的位置相结合。
    • 9. 发明授权
    • Process for cracking a heavy hydrocarbon feedstream
    • 裂解重烃进料流的方法
    • US08684384B2
    • 2014-04-01
    • US12437063
    • 2009-05-07
    • David B. SpicerCaleb M. SchererJames M. FryeSubramanian Annamalai
    • David B. SpicerCaleb M. SchererJames M. FryeSubramanian Annamalai
    • C10G9/16
    • C10G9/16
    • A process for cracking a hydrocarbon feedstream containing non-volatile components in a hydrocarbon cracking furnace having upper and lower convection heating sections within a flue of the furnace, a radiant heating section downstream of and connected to said lower convection heating section, a transfer line exchanger downstream of and connected to said radiant heating section, a furnace box containing furnace burners and said radiant heating section, and a vapor/liquid separator vessel connected between the upper and lower convection heating sections, the process comprising (a) passing said hydrocarbon feedstream into said upper convection section to heat said hydrocarbon feedstream to a first temperature sufficient to flash at least a portion of the hydrocarbons within said hydrocarbon feedstream into a vapor phase to form a vapor/liquid stream; (b) passing said vapor/liquid stream out of said upper convection section and into said vapor/liquid separator to separate said vapor/liquid stream into a hydrocarbon-containing vapor phase and a hydrocarbon-containing liquid phase within said vapor/liquid separator; (c) collecting said liquid phase into a bottoms liquid within said vapor/liquid separator; (d) passing said vapor phase into said radiant heating section and cracking hydrocarbons in said vapor phase to form an olefins-containing effluent stream; and (e) periodically injecting an air-steam mixture into said convection heating section, then through said vapor/liquid separator to incinerate coke formed and passing an incinerated coke residue/air-steam mixture so-formed between the furnace burners within the furnace box.
    • 一种在炉内烟道内具有上下对流加热段的碳氢化合物裂解炉中含有非挥发成分的烃类原料流裂化的方法,下游对流加热段下游并与之连接的辐射加热段, 在所述辐射加热部分的下游并连接到所述辐射加热部分,包含炉燃烧器和所述辐射加热部分的炉箱以及连接在上部和下部对流加热部分之间的蒸气/液体分离器容器,所述方法包括(a)使所述烃进料流进入 所述上对流部分将所述烃进料流加热至足以将所述烃进料流中的至少一部分烃闪蒸成气相以形成蒸气/液体流的第一温度; (b)使所述蒸汽/液体流从所述上部对流部分流出并进入所述气/液分离器,以将所述气/液流分离成所述气/液分离器内的含烃气相和含烃液相; (c)将所述液相收集到所述蒸汽/液体分离器内的底部液体中; (d)将所述气相通入所述辐射加热段,并在所述气相中裂解烃,以形成含烯烃的流出物流; 然后通过所述蒸汽/液体分离器周期性地将空气 - 蒸汽混合物注入到所述对流加热部分中,以焚烧所形成的焦炭并通过炉内燃烧器之间形成的焚烧焦炭残渣/空气 - 蒸汽混合物 。
    • 10. 发明申请
    • Process for Cracking a Heavy Hydrocarbon Feedstream
    • 破碎重烃进料流的方法
    • US20100174130A1
    • 2010-07-08
    • US12437063
    • 2009-05-07
    • David B. SpicerCaleb M. SchererJames M. FryeSubramanian Annamalai
    • David B. SpicerCaleb M. SchererJames M. FryeSubramanian Annamalai
    • C07C4/02B01J19/00
    • C10G9/16
    • A process for cracking a hydrocarbon feedstream containing non-volatile components in a hydrocarbon cracking furnace having upper and lower convection heating sections within a flue of the furnace, a radiant heating section downstream of and connected to said lower convection heating section, a transfer line exchanger downstream of and connected to said radiant heating section, a furnace box containing furnace burners and said radiant heating section, and a vapor/liquid separator vessel connected between the upper and lower convection heating sections, the process comprising (a) passing said hydrocarbon feedstream into said upper convection section to heat said hydrocarbon feedstream to a first temperature sufficient to flash at least a portion of the hydrocarbons within said hydrocarbon feedstream into a vapor phase to form a vapor/liquid stream; (b) passing said vapor/liquid stream out of said upper convection section and into said vapor/liquid separator to separate said vapor/liquid stream into a hydrocarbon-containing vapor phase and a hydrocarbon-containing liquid phase within said vapor/liquid separator; (c) collecting said liquid phase into a bottoms liquid within said vapor/liquid separator; (d) passing said vapor phase into said radiant heating section and cracking hydrocarbons in said vapor phase to form an olefins-containing effluent stream; and (e) periodically injecting an air-steam mixture into said convection heating section, then through said vapor/liquid separator to incinerate coke formed and passing an incinerated coke residue/air-steam mixture so-formed between the furnace burners within the furnace box.
    • 一种在炉内烟道内具有上下对流加热段的碳氢化合物裂解炉中含有非挥发成分的烃类原料流裂化的方法,下游对流加热段下游并与之连接的辐射加热段, 在所述辐射加热部分的下游并连接到所述辐射加热部分,包含炉燃烧器和所述辐射加热部分的炉箱以及连接在上部和下部对流加热部分之间的蒸气/液体分离器容器,所述方法包括(a)使所述烃进料流进入 所述上对流部分将所述烃进料流加热至足以将所述烃进料流中的至少一部分烃闪蒸成气相以形成蒸气/液体流的第一温度; (b)使所述蒸汽/液体流从所述上部对流部分流出并进入所述气/液分离器,以将所述气/液流分离成所述气/液分离器内的含烃气相和含烃液相; (c)将所述液相收集到所述蒸汽/液体分离器内的底部液体中; (d)将所述气相通入所述辐射加热段,并在所述气相中裂解烃,以形成含烯烃的流出物流; 然后通过所述蒸汽/液体分离器周期性地将空气 - 蒸汽混合物注入到所述对流加热部分中,以焚烧所形成的焦炭并通过炉内燃烧器之间形成的焚烧焦炭残渣/空气 - 蒸汽混合物 。