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1. 发明申请

WO2007102032A2 TWO-STAGE COMBINED COCURRENT-COUNTERCURRENT GASIFIER 审中-公开
标题翻译：两级组合式电流相对放电器
公开(公告)号：WO2007102032A2
公开(公告)日：2007-09-13
申请号：PCT/GR2007/000017
申请日：2007-03-06
申请人： ELEFSINIOTIS, Lampros
发明人： ELEFSINIOTIS, Lampros
IPC分类号： C10J3/26 , C10J3/20
CPC分类号： C10J3/26 , C10J3/20 , C10J3/721 , C10J2200/09 , C10J2300/0916 , C10J2300/0956 , C10J2300/1207 , C10J2300/1215 , C10J2300/1223
摘要： Two-stage combined cocurrent-countercurrent gasifier, which is used for the thermochemical process that converts solid carbonaceous materials into combustible gases, has as first (pyrolysis) stage a countercurrent reactor (1) placed above the second (gasification) stage which is a cocurrent reactor (2) and is characterized in that between the two stages a diaphragm (3) is present, which cuts off the gaseous flow between the countercurrent reactor (1) and the cocurrent reactor (2), while allowing the solid pieces falling from the countercurrent reactor (1) to pass to the cocurrent reactor (2). From the measurements of the physical parameters at the discharge (11) of the pyrolysis gases (vapor, volatiles) we have an immediate image of the composition and/or the humidity of the new incoming fuel, thus the automatic control and the safe operation of the process are achieved by setting the air and/or fuel feed of the countercurrent reactor. Thereby variations in the composition and/or humidity of the incoming fuel are balanced and settled quantities of charcoal and gases are supplied to the next process stages, thus it is easy to control all the gasification process. The burning torch (12) of gases coming from the countercurrent reactor (1), is placed so that to introduce the flame into the cocurrent reactor (2) by horizontal setting. The upper part (14) of the cocurrent reactor (2) is configured so that to expand the flue gases of the burning torch (12) by cyclonic mode.
摘要翻译：用于将固体碳质材料转化为可燃气体的热化学工艺的两级组合并流逆流气化器具有放置在第二（气化）级上方的逆流反应器（1）的第一（热解）阶段，其是并流的反应器（2），其特征在于，在两个阶段之间存在隔膜（3），其隔断逆流反应器（1）和并流反应器（2）之间的气流，同时允许固体件从逆流反应器（1）通过并流反应器（2）。从热解气体（蒸汽，挥发物）排放物（11）的物理参数的测量可以看出，新进入燃料的组成和/或湿度立即显现，因此可以自动控制和安全运行该过程通过设置逆流反应器的空气和/或燃料进料来实现。因此，进入燃料的组成和/或湿度的变化是平衡的，并且将稳定的量的木炭和气体供应到下一个工艺阶段，因此容易控制所有的气化过程。来自逆流反应器（1）的气体燃烧的炬（12）被放置成通过水平设置将火焰引入并流电抗器（2）中。并流反应器（2）的上部（14）被配置成通过气旋模式来扩大燃烧的炬（12）的烟气。

2. 发明申请

WO2008107727A3 THREE-STAGE GASIFIER, FIXED BED, WHICH HAS BUFFER ZONE OF GASEOUS FLOW BETWEEN PYROLYSIS ZONE AND COMBUSTION ZONE 审中-公开
公开(公告)号：WO2008107727A3
公开(公告)日：2008-09-12
申请号：PCT/GR2008/000017
申请日：2008-03-04
申请人： ELEFSINIOTIS, Lampros
发明人： ELEFSINIOTIS, Lampros
IPC分类号： C10J3/66 , C10J3/24
摘要： At the upper place of the gasifier exists the first stage which is the pyrolysis zone (1) and it is a countercurrent reactor. At the middle place exists the second stage which is the combustion zone (2). At the bottom place exists the third stage which is the gasification zone (3) and it is a cocurrent reactor. Figure 1 shows the normal operation of the buffer zone (20) and figure 2 shows the reversed operation of the buffer zone (20). The three-stage gasifier is characterized from the fact that the passage from the normal operation of the buffer zone (20) to the reversed operation of the buffer zone (20) and vice versa is achieved only by proper rotation settings of the pumps (BPA), (BCA), (BPG), (BGO), so creating a new model of gaseous flow management between the three stages of the gasifier. This model can achieve the simultaneous combination of the following advantages: -Industrial scale safe operation ability, by using fuel with big possible variations in humidity and/or composition. -The producer gas is free of harmful components (tars, dioxins). -The gasifier does not expose its moving mechanical parts at temperatures above 750°C. -There is not any moving seal mechanism between the stages of the gasifier.

3. 发明申请

WO2008107727A2 THREE-STAGE GASIFIER, FIXED BED, WHICH HAS BUFFER ZONE OF GASEOUS FLOW BETWEEN PYROLYSIS ZONE AND COMBUSTION ZONE 审中-公开
标题翻译：三级气化器，固定床，已经缓解了热解区和燃烧区之间的气体流动区
公开(公告)号：WO2008107727A2
公开(公告)日：2008-09-12
申请号：PCT/GR2008000017
申请日：2008-03-04
申请人： ELEFSINIOTIS LAMPROS
发明人： ELEFSINIOTIS LAMPROS
IPC分类号： C10J3/66 , C10J3/24
CPC分类号： C10J3/20 , C10J3/26 , C10J3/721 , C10J2200/09 , C10J2300/0916 , C10J2300/0956 , C10J2300/1207 , C10J2300/1215 , C10J2300/1223 , Y02P20/129
摘要： At the upper place of the gasifier exists the first stage which is the pyrolysis zone (1) and it is a countercurrent reactor. At the middle place exists the second stage which is the combustion zone (2). At the bottom place exists the third stage which is the gasification zone (3) and it is a cocurrent reactor. Figure 1 shows the normal operation of the buffer zone (20) and figure 2 shows the reversed operation of the buffer zone (20). The three-stage gasifier is characterized from the fact that the passage from the normal operation of the buffer zone (20) to the reversed operation of the buffer zone (20) and vice versa is achieved only by proper rotation settings of the pumps (BPA), (BCA), (BPG), (BGO), so creating a new model of gaseous flow management between the three stages of the gasifier. This model can achieve the simultaneous combination of the following advantages: -Industrial scale safe operation ability, by using fuel with big possible variations in humidity and/or composition. -The producer gas is free of harmful components (tars, dioxins). -The gasifier does not expose its moving mechanical parts at temperatures above 750°C. -There is not any moving seal mechanism between the stages of the gasifier.
摘要翻译：在气化炉的上部存在作为热解区（1）的第一阶段，它是逆流反应器。在中间位置是燃烧区的第二阶段（2）。在底部存在作为气化区（3）的第三阶段，它是并流反应器。图1显示了缓冲区（20）的正常操作，图2显示缓冲区（20）的反向操作。三级气化器的特征在于，从缓冲区（20）的正常操作到缓冲区（20）的反向操作（反之亦然）的通过仅通过泵的适当的旋转设置（BPA ），（BCA），（BPG），（BGO），因此在气化器的三个阶段之间创建一个新的气体流量管理模型。该模式可以实现以下优点的同时组合： - 工业规模的安全操作能力，通过使用具有很大可能变化的湿度和/或组成的燃料。 - 生产的天然气不含有害成分（焦油，二恶英）。 - 气化器在高于750°C的温度下不会暴露其移动的机械部件。 - 气化器阶段之间没有任何移动的密封机构。

4. 发明申请

WO2007102032A3 TWO-STAGE COMBINED COCURRENT-COUNTERCURRENT GASIFIER 审中-公开
标题翻译：两级组合式电流相对放电器
公开(公告)号：WO2007102032A3
公开(公告)日：2008-02-07
申请号：PCT/GR2007000017
申请日：2007-03-06
申请人： ELEFSINIOTIS LAMPROS
发明人： ELEFSINIOTIS LAMPROS
IPC分类号： C10J3/26 , C10J3/20
CPC分类号： C10J3/26 , C10J3/20 , C10J3/721 , C10J2200/09 , C10J2300/0916 , C10J2300/0956 , C10J2300/1207 , C10J2300/1215 , C10J2300/1223
摘要： Two-stage combined cocurrent-countercurrent gasifier, which is used for the thermochemical process that converts solid carbonaceous materials into combustible gases, has as first (pyrolysis) stage a countercurrent reactor (1) placed above the second (gasification) stage which is a cocurrent reactor (2) and is characterized in that between the two stages a diaphragm (3) is present, which cuts off the gaseous flow between the countercurrent reactor (1) and the cocurrent reactor (2), while allowing the solid pieces falling from the countercurrent reactor (1) to pass to the cocurrent reactor (2). From the measurements of the physical parameters at the discharge (11) of the pyrolysis gases (vapor, volatiles) we have an immediate image of the composition and/or the humidity of the new incoming fuel, thus the automatic control and the safe operation of the process are achieved by setting the air and/or fuel feed of the countercurrent reactor. Thereby variations in the composition and/or humidity of the incoming fuel are balanced and settled quantities of charcoal and gases are supplied to the next process stages, thus it is easy to control all the gasification process. The burning torch (12) of gases coming from the countercurrent reactor (1), is placed so that to introduce the flame into the cocurrent reactor (2) by horizontal setting. The upper part (14) of the cocurrent reactor (2) is configured so that to expand the flue gases of the burning torch (12) by cyclonic mode.
摘要翻译：用于将固体碳质材料转化为可燃气体的热化学工艺的两级组合并流逆流气化器具有放置在第二（气化）级上方的逆流反应器（1）的第一（热解）阶段，其是并流的反应器（2），其特征在于，在两个阶段之间存在隔膜（3），其隔断逆流反应器（1）和并流反应器（2）之间的气流，同时允许固体件从逆流反应器（1）通过并流反应器（2）。从热解气体（蒸汽，挥发物）排放物（11）的物理参数的测量可以看出，新进入燃料的组成和/或湿度立即显现，因此可以自动控制和安全运行该过程通过设置逆流反应器的空气和/或燃料进料来实现。因此，进入燃料的组成和/或湿度的变化是平衡的，并且将稳定的量的木炭和气体供应到下一个工艺阶段，因此容易控制所有的气化过程。来自逆流反应器（1）的气体燃烧的炬（12）被放置成通过水平设置将火焰引入并流电抗器（2）中。并流反应器（2）的上部（14）被配置成通过气旋模式来扩大燃烧的炬（12）的烟气。

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