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1. 发明申请

US20150183961A1 Biomass Processing 审中-公开
标题翻译：生物质处理
公开(公告)号：US20150183961A1
公开(公告)日：2015-07-02
申请号：US14510298
申请日：2014-10-09
申请人： Mahesh Talwar
发明人： Mahesh Talwar
IPC分类号： C08K9/00 , C10L1/02 , C08L95/00 , C10L1/182
CPC分类号： C08L95/00 , C08L91/00 , C08L2555/62 , C09D191/00 , C10B47/44 , C10B53/02 , C10B57/02 , C10K1/101 , C10L1/02 , C10L1/1824 , C10L9/083 , C10L2200/0469 , C10L2290/08 , C10L2290/24 , Y02E50/14 , Y02E50/15 , Y02E50/32 , Y02P20/145
摘要： A biomass processing system produces a refined bio oil. The system includes a first auger carrying the biomass through a torrefaction/drying chamber to dry the biomass and a second auger carries biomass feed material though the torrefaction/drying chamber to produce vapor phase bio oil. The vapor phase bio oil is collected carried from the torrefaction/drying chamber to condensers and quenched by a water spray before release into the condensers. The water spray also serving as a solvent to reduce pH in the liquid phase raw bio oil. The raw bio oil is carried to a conditioning system where the raw bio oil resides in a separation tank where the water separates and is removed producing refined bio oil. Ethanol may be mixed with the refined bio oil to produce fuel oil or petroleum asphalt may be mixed with the refined bio to obtain a substitute for road asphalt.
摘要翻译：生物质处理系统生产精制生物油。该系统包括通过烘焙/干燥室携带生物质以干燥生物质的第一螺旋推运器，并且第二螺旋钻通过烘焙/干燥室运送生物质进料，以产生气相生物油。将蒸气相生物油从烘焙/干燥室收集到冷凝器，并在释放到冷凝器之前通过喷水骤冷。水喷雾也用作溶剂以降低液相生物油中的pH。原始生物油被运送到一个调节系统中，其中生物生物油存在于分离槽中，在该分离槽中水被分离并被除去产生精制生物油。乙醇可与精制生物油混合生产燃料油，或石油沥青可与精制生物混合，以获得道路沥青的替代品。

2. 发明申请

US20160060555A1 Method to Produce Charcoal Without Producing Bio Oil Through Pyrolysis of Woody Biomass 审中-公开
标题翻译：通过木质生物质热解生产生物油的方法
公开(公告)号：US20160060555A1
公开(公告)日：2016-03-03
申请号：US14935620
申请日：2015-11-09
申请人： Mahesh Talwar
发明人： Mahesh Talwar
IPC分类号： C10L5/36 , C10L9/08 , C10L5/14
CPC分类号： C10L5/361 , C08L91/00 , C08L95/00 , C08L2555/62 , C09D191/00 , C10B47/44 , C10B53/02 , C10B57/02 , C10K1/101 , C10L1/02 , C10L5/14 , C10L5/447 , C10L9/083 , C10L2200/0469 , C10L2290/08 , C10L2290/24 , Y02E50/10 , Y02E50/14 , Y02E50/15 , Y02E50/30 , Y02P20/145
摘要： A biomass processing system produces charcoal briquettes in a closed loop system. The system includes a first and second torrefaction/drying augers drying green raw sawdust and providing the dried material to a carbonizing auger. Charcoal released from the carbonizing auger is formed into charcoal briquettes. Process gas created during the charcoal production is used to provide heat required by the process.
摘要翻译：生物质处理系统在闭环系统中生产木炭块。该系统包括第一和第二烘干/干燥螺旋钻干燥绿色原料锯末，并将干燥的材料提供给碳化螺旋钻。从碳化螺旋钻释放的木炭被形成为木炭块。在炭生产过程中产生的过程气体用于提供该过程所需的热量。

3. 发明申请

US20110016772A1 Acid Esterification Through Nano Reactor 审中-公开
标题翻译：通过纳米反应器进行酸酯化
公开(公告)号：US20110016772A1
公开(公告)日：2011-01-27
申请号：US12509346
申请日：2009-07-24
申请人： Mahesh Talwar
发明人： Mahesh Talwar
IPC分类号： C10L1/18 , B01J19/00
CPC分类号： B01J19/0093 , B01F5/0256 , B01F2215/0468 , B01J2219/00788 , B01J2219/00864 , B01J2219/00873 , B01J2219/00889 , C10L1/026 , Y02E50/13
摘要： A biodiesel generation system incorporates acid esterification through a hydro-cavitation based nano reactor. A feed material is a mixture of approximately 30 percent Palm Fatty Acid Distillate (PFAD) mixed with Para Toluene Sulfonic Acid (PTSA) as an acid catalyst and methanol as a reagent. The PFAD is approximately 90 percent Free Fatty Acid (FFA) resulting in the feed material being approximately 27 percent FFA. The acid catalyst in the feed material facilitates an esterification process to produce biodiesel. The feed material is pumped through the hydro-cavitation based nano reactor and forced through a nano orifice where, by a phenomenon of hydro cavitation, collapsing nano liquid molecules can generate instantaneous temperatures of 1000 degrees centigrade resulting in quick reaction taking place at the surface of collapsing nano molecules. Partially reacted feed material may be recycled through the nano reactor several times to complete the reaction.
摘要翻译：生物柴油生成系统通过基于加氢气蚀的纳米反应器引入酸酯化。进料是与作为酸催化剂的对甲苯磺酸（PTSA）和甲醇作为试剂混合的约30％的棕榈酸脂肪酸馏分（PFAD）的混合物。 PFAD约为90％的游离脂肪酸（FFA），导致饲料的FFA约为27％。进料中的酸催化剂促进了酯化过程以产生生物柴油。进料材料被泵送通过基于加氢气穴的纳米反应器并且被迫通过纳米孔口，其中通过水力气蚀的现象，塌陷的纳米液体分子可以产生1000摄氏度的瞬时温度，导致快速反应发生在崩溃的纳米分子。部分反应的进料可以通过纳米反应器多次循环以完成反应。

4. 发明申请

US20150184025A1 Biomass Bio Oil Upgrade Method 审中-公开
标题翻译：生物质生物油升级方法
公开(公告)号：US20150184025A1
公开(公告)日：2015-07-02
申请号：US14140956
申请日：2013-12-26
申请人： Mahesh Talwar
发明人： Mahesh Talwar
IPC分类号： C09D195/00 , C09D191/00 , C08L95/00
CPC分类号： C09D191/00 , C08L91/00 , C08L95/00 , C08L2555/62
摘要： A bio oil pyrolysis and conditioning system produces a useful road asphalt. The pyrolysis system includes an auger carrying biomass feed material though an oxygen rare pyrolysis chamber. Vapor phase bio oil is collected at three locations along the length of the pyrolysis chamber and carried from the pyrolysis chamber to condensers and quenched by a water spray before release into the condensers. The water also serving as a solvent to reduce pH in the liquid phase raw bio oil. The raw bio oil is carried to a conditioning system where the raw bio oil resides in a separation tank where the water separates and is removed producing refined bio oil. The refined bio oil is mixed with an equal or greater amount of petroleum asphalt to obtain a substitute for road asphalt.
摘要翻译：生物油热解和调节系统生产有用的道路沥青。热解系统包括通过氧稀有热解室携带生物质进料的螺旋推运器。蒸气相生物油在热解室长度的三个位置收集，并从热解室运送到冷凝器，并通过喷水骤冷，然后释放到冷凝器中。水也用作溶剂以降低液相生物生物油中的pH。原始生物油被运送到一个调节系统中，其中生物生物油存在于分离槽中，在该分离槽中水被分离并被除去产生精制生物油。精炼的生物油与等量或更多量的石油沥青混合以获得道路沥青的替代品。

5. 发明申请

US20110253103A1 Tug Boat Engine Emissions Control Suite 审中-公开
标题翻译：拖船发动机排放控制套件
公开(公告)号：US20110253103A1
公开(公告)日：2011-10-20
申请号：US12840254
申请日：2010-07-20
申请人： Mahesh Talwar , Francois Bernard
发明人： Mahesh Talwar , Francois Bernard
IPC分类号： F02D7/00
CPC分类号： F02M53/02 , F02D41/401 , F02D2250/36 , F02D2250/38 , F02M57/023 , F02M59/26 , F02M59/265 , Y02T10/44
摘要： A tug boat diesel engine emissions control suite includes modified fuel injectors including a fuel injection timing retard feature, and diesel fuel heating. Tug boats are now required to comply with USEPA emission standards under 40 CFR Part 94 regulations. Retarding the fuel injection timing reduces peak temperatures during combustion which in turn reduces production of Nitrogen Oxides (NOx) but also increases emissions of particulate matter (PM), Carbon Monoxide (CO), and Hydrocarbons (HC) in the exhaust. Heating the diesel fuel provides a reduction in increased PM, CO, and HC to acceptable levels. Experiments showed that a novel modification to a plunger in the fuel injectors providing up to six degrees of fuel injection timing retarding, and fuel heated to 120 to 140 degrees Fahrenheit, resulted in meeting the 40 CFR Part 94 regulations.
摘要翻译：拖船柴油发动机排放控制套件包括改进的燃料喷射器，包括燃料喷射正时延迟特征和柴油燃料加热。拖船现在需要遵守40 CFR Part 94规定的USEPA排放标准。燃料喷射时间的延迟降低了燃烧期间的峰值温度，从而降低了氮氧化物（NOx）的产生，同时也增加了废气中的颗粒物质（一氧化碳）和一氧化碳（HC）的排放。加热柴油可以将PM，CO和HC的增加降低到可接受的水平。实验表明，对燃料喷射器中的柱塞进行新颖的修改，提供高达六度的燃料喷射正时延迟，并将燃料加热至120至140华氏度，从而达到40 CFR Part 94的规定。

6. 发明申请

US20110253074A1 Locomotive Engine Emissions Control Suite 审中-公开
标题翻译：机车发动机排放控制套件
公开(公告)号：US20110253074A1
公开(公告)日：2011-10-20
申请号：US12759890
申请日：2010-04-14
申请人： Mahesh Talwar , Francois Bernard
发明人： Mahesh Talwar , Francois Bernard
IPC分类号： F01P7/14 , F02G5/00 , F02M69/04 , F02P5/04
CPC分类号： F02M31/10 , F01P2060/10 , F02D41/401 , F02M53/02 , F02M57/023 , Y02T10/126 , Y02T10/44
摘要： A locomotive diesel engine emissions control suite includes retarding fuel injection timing and heating the diesel fuel. Switch locomotives are now required to comply with USEPA emission standards under 40 CFR Part 1033 regulations. Retarding the fuel injection timing reduces peak temperatures during combustion which in turn reduces production of Nitrogen oxides (NOx) but also increases emissions of particulate matter (PM), Carbon Monoxide (CO), and Hydrocarbons (HC) in the exhaust. Unrelated efforts to reduce the smoke in diesel exhaust by pre-heating the diesel fuel showed an unexpected reduction in PM, CO, and HC. Such heating of the diesel fuel did not affect the reduction in NOx but reduced emissions of PM, CO, and HC to acceptable levels. Further experiments showed that two degrees of fuel injection retarding and fuel heated to 120 to 140 degrees Fahrenheit resulted in meeting the 40 CFR Part 1033 regulations.
摘要翻译：机车柴油机排放控制套件包括延迟燃油喷射正时和加热柴油。开关机车现在需要符合40 CFR Part 1033规定中的USEPA排放标准。燃料喷射时间的延迟降低了燃烧期间的峰值温度，从而降低了氮氧化物（NOx）的产生，同时也增加了废气中颗粒物质（一氧化碳）和一氧化碳（HC）的排放。通过预热柴油燃料来减少柴油机排气烟雾的不相关努力显示出PM，CO和HC意外减少。柴油的这种加热不会影响NOx的减少，而是将PM，CO和HC的排放减少到可接受的水平。进一步的实验表明，两度燃料喷射阻燃和燃料加热到120华氏度至140华氏度，导致符合40 CFR Part 1033规定。

7. 发明授权

US09631155B2 Method to produce charcoal without producing bio oil through pyrolysis of woody biomass 有权
公开(公告)号：US09631155B2
公开(公告)日：2017-04-25
申请号：US14935620
申请日：2015-11-09
申请人： Mahesh Talwar
发明人： Mahesh Talwar
IPC分类号： C10B47/00 , C10L5/36 , C10L5/14 , C10L9/08 , C10K1/10 , C10L1/02 , C09D191/00 , C10B47/44 , C10B53/02 , C10B57/02 , C08L91/00 , C08L95/00 , C10L5/44 , C10L5/00
CPC分类号： C10L5/361 , C08L91/00 , C08L95/00 , C08L2555/62 , C09D191/00 , C10B47/44 , C10B53/02 , C10B57/02 , C10K1/101 , C10L1/02 , C10L5/14 , C10L5/447 , C10L9/083 , C10L2200/0469 , C10L2290/08 , C10L2290/24 , Y02E50/10 , Y02E50/14 , Y02E50/15 , Y02E50/30 , Y02P20/145
摘要： A biomass processing system produces charcoal briquettes in a closed loop system. The system includes a first and second torrefaction/drying augers drying green raw sawdust and providing the dried material to a carbonizing auger. Charcoal released from the carbonizing auger is formed into charcoal briquettes. Process gas created during the charcoal production is used to provide heat required by the process.

8. 发明申请

US20150184098A1 Biomass Bio Oil Upgrade Method 审中-公开
标题翻译：生物质生物油升级方法
公开(公告)号：US20150184098A1
公开(公告)日：2015-07-02
申请号：US14140766
申请日：2013-12-26
申请人： Mahesh Talwar
发明人： Mahesh Talwar
IPC分类号： C10L1/18
CPC分类号： C10L1/02 , C10B47/44 , C10B53/02 , C10B57/02 , C10K1/06 , C10L2290/02 , C10L2290/06 , C10L2290/50 , C10L2290/52 , C10L2290/54 , Y02E50/14 , Y02E50/32 , Y02P20/145
摘要： A bio oil pyrolysis and conditioning system produces a useful fuel oil. The pyrolysis system includes an auger carrying biomass feed material though an oxygen rare pyrolysis chamber. Vapor phase bio oil is collected at three locations along the length of the pyrolysis chamber and carried from the pyrolysis chamber to condensers and quenched by a water spray before release into the condensers. The water also serving as a solvent to reduce pH in the liquid phase raw bio oil. The raw bio oil is carried to a conditioning system where the raw bio oil resides in a separation tank where the water separates and is removed producing refined bio oil. Ethanol is mixed with the refined bio oil to provide the fuel oil.
摘要翻译：生物油热解和调节系统产生有用的燃料油。热解系统包括通过氧稀有热解室携带生物质进料的螺旋推运器。蒸气相生物油在热解室长度的三个位置收集，并从热解室运送到冷凝器，并通过喷水骤冷，然后释放到冷凝器中。水也用作溶剂以降低液相生物生物油中的pH。原始生物油被运送到一个调节系统中，其中生物生物油存在于分离槽中，在该分离槽中水被分离并被除去产生精制生物油。将乙醇与精制生物油混合以提供燃料油。

9. 发明申请

US20100107474A1 Apparatus and method for Rapid Biodiesel Fuel Production 审中-公开
标题翻译：快速生物柴油燃料生产的装置和方法
公开(公告)号：US20100107474A1
公开(公告)日：2010-05-06
申请号：US12262942
申请日：2008-10-31
申请人： Mahesh Talwar , Jagroop S. Gill , Angelo C. Piro, JR.
发明人： Mahesh Talwar , Jagroop S. Gill , Angelo C. Piro, JR.
IPC分类号： C10L1/18 , B01J19/00
CPC分类号： B01J19/008 , B01J8/20 , B01J19/26 , B01J2219/00006 , B01J2219/0004 , B01J2219/00164 , B01J2219/30215 , C10G2300/1011 , C10L1/026 , Y02E50/13 , Y02P30/20
摘要： Apparatus and method for rapid production of biodiesel fuel. The apparatus includes a packed column followed by a high pressure kinetic reactor. A homogeneous stream of feed oil (vegetable oil or animal fat), methanol, and a catalyst is metered, mixed, fed into a packed column, and finally into the high pressure kinetic reactor where the conversion into biodiesel fuel is completed. The packed column is packed with rings (either Raschig rings or pall rings or equivalent). The homogeneous stream enters from the bottom with rings kept in a fluidized bed state to allow greatest surface area for reaction to take place. Approximately 40 to 70 percent reaction is typically achieved in the packed column. The high pressure kinetic reactor receives the partially reacted homogeneous stream and breaks fluid molecules into nano molecules with very high instantaneous temperatures and availability of large surface areas which allow complete reaction without external heat.
摘要翻译：快速生产生物柴油燃料的设备和方法。该装置包括一个填充柱，随后是高压动力反应器。将均匀的原料油（植物油或动物脂肪），甲醇和催化剂计量，混合，进料到填充柱中，最后进入转化为生物柴油燃料的高压动力反应器中。填充柱填充有环（Raschig环或pall环或等效物）。均匀的流体从底部进入，其中环保持在流化床状态，以允许最大的表面积进行反应。通常在填充柱中实现约40至70％的反应。高压动力反应器接收部分反应的均匀流，并将流体分子分解成具有非常高的瞬时温度和大的表面积的可用性的纳米分子，其允许没有外部热量的完全反应。

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