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公开(公告)号:WO2011159686A3
公开(公告)日:2012-03-08
申请号:PCT/US2011040327
申请日:2011-06-14
Applicant: PENMAN ROBERT R
Inventor: PENMAN ROBERT R
CPC classification number: F02M27/02 , F02B43/04 , F02B51/02 , F02M25/12 , F02M31/18 , Y02T10/126 , Y02T10/32
Abstract: A fuel reforming system, process, and device including a catalytic chamber and a heating chamber. The catalytic chamber, further including a fluid fuel intake and a gaseous fluid exit port and at least one heat exchanger for distributing heat between the heating chamber and the catalytic chamber. The catalytic chamber further including a screen member having a surface, wherein the member includes a catalytic deposit made from a combination of platinum and rhodium alloy. A catalytic conversion of converting liquid fuel to gaseous fuel occurs within the catalytic chamber. Fuel exits the fuel reforming device through a gaseous fluid exit port.
Abstract translation: 一种燃料重整系统,工艺和装置,包括催化室和加热室。 催化室还包括流体燃料进口和气体流体出口以及用于在加热室和催化室之间分配热量的至少一个热交换器。 所述催化室还包括具有表面的筛网构件,其中所述构件包括由铂和铑合金的组合制成的催化沉积物。 在催化室内发生将液体燃料转化为气体燃料的催化转化。 燃料通过气态流体出口离开燃料重整装置。
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公开(公告)号:WO2012106400A2
公开(公告)日:2012-08-09
申请号:PCT/US2012023441
申请日:2012-02-01
Applicant: PENMAN ROBERT R
Inventor: PENMAN ROBERT R
CPC classification number: F02B43/04 , F02B51/02 , F02D19/0605 , F02D19/0628 , F02D19/0642 , F02D19/0671 , F02D19/081 , F02M25/12 , F02M27/02 , F02M31/18 , Y02T10/126 , Y02T10/32 , Y02T10/36
Abstract: A fuel reforming system, process, and device including a catalytic chamber and a heating chamber. The catalytic chamber, further including a fluid fuel intake and a gaseous fluid exit port and at least one heat exchanger for distributing heat between the heating chamber and the catalytic chamber. The catalytic chamber further including a screen member having a surface, wherein the member includes a catalytic deposit made from a combination of platinum and rhodium alloy. A catalytic conversion of converting liquid fuel to gaseous fuel occurs within the catalytic chamber. Fuel exits the fuel reforming device through a gaseous fluid exit port. In the process of phase change from liquid to gaseous phase, there is no change of chemical composition and C8H18 remains stable throughout., except for an increase in Enthalpy (heat content) per mol.
Abstract translation: 包括催化室和加热室的燃料重整系统,方法和装置。 催化室还包括流体燃料入口和气态流体出口以及用于在加热室和催化室之间分配热量的至少一个热交换器。 所述催化室还包括具有表面的筛网构件,其中所述构件包括由铂和铑合金的组合制成的催化沉积物。 在催化室内发生将液体燃料转化为气体燃料的催化转化。 燃料通过气态流体出口离开燃料重整装置。 在从液相到气相的相变过程中,除了每摩尔焓(热含量)的增加外,化学组成的变化并且C8H18在整个过程中保持稳定。
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公开(公告)号:WO2009055372A2
公开(公告)日:2009-04-30
申请号:PCT/US2008080618
申请日:2008-10-21
Applicant: PENMAN ROBERT R
Inventor: PENMAN ROBERT R
CPC classification number: F02B43/04 , F02B51/02 , F02M25/12 , F02M27/02 , F02M31/18 , Y02T10/126 , Y02T10/32
Abstract: A fuel reforming system, process, and device including a catalytic chamber and a heating chamber. The catalytic chamber, further including a fluid fuel intake and a gaseous fluid exit port and at least one heat exchanger for distributing heat between the heating chamber and the catalytic chamber. The catalytic chamber further including a screen member having a surface, wherein the member includes a catalytic deposit made from a combination of platinum and rhodium alloy. A catalytic conversion of converting liquid fuel to gaseous fuel occurs within the catalytic chamber. Fuel exits the fuel reforming device through a gaseous fluid exit port.
Abstract translation: 一种燃料重整系统,工艺和装置,包括催化室和加热室。 催化室还包括流体燃料进口和气体流体出口以及用于在加热室和催化室之间分配热量的至少一个热交换器。 所述催化室还包括具有表面的筛网构件,其中所述构件包括由铂和铑合金的组合制成的催化沉积物。 在催化室内发生将液体燃料转化为气体燃料的催化转化。 燃料通过气态流体出口离开燃料重整装置。
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