公开(公告)号：US09242219B2

公开(公告)日：2016-01-26

申请号：US13361582

申请日：2012-01-30

申请人： Douglas R. Bull ,  Ross M. Patten ,  Paul Cairney ,  Gerald M. Cox ,  William P. Jepson

发明人： Douglas R. Bull ,  Ross M. Patten ,  Paul Cairney ,  Gerald M. Cox ,  William P. Jepson

IPC分类号： B01J7/00 ,  B01J8/18 ,  C10J3/48 ,  C02F11/10 ,  C10K1/02 ,  C02F11/12

CPC分类号： C10J3/466 ,  B01J8/1809 ,  B01J8/1827 ,  B01J2208/00893 ,  B01J2208/00902 ,  C02F11/10 ,  C02F11/12 ,  C02F11/121 ,  C10J3/482 ,  C10J3/84 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0956 ,  C10J2300/1643 ,  C10J2300/1807 ,  C10K1/026 ,  Y02P20/129 ,  Y02W10/40 ,  Y10T29/49

摘要： A fluidized bed biogasifier is provided for gasifying biosolids. The biogasifier includes a reactor vessel and a feeder for feeding biosolids into the reactor vessel at a desired feed rate during steady-state operation of the biogasifier. A fluidized bed in the base of the reactor vessel has a cross-sectional area that is proportional to at least the fuel feed rate such that the superficial velocity of gas is in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). In a method for gasifying biosolids, biosolids are fed into a fluidized bed reactor. Oxidant gases are applied to the fluidized bed reactor to produce a superficial velocity of producer gas in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). The biosolids are heated inside the fluidized bed reactor to a temperature range between 900° F. (482.2° C.) and 1700° F. (926.7° C.) in an oxygen-starved environment having a sub-stoichiometric oxygen level, whereby the biosolids are gasified.

摘要翻译： 提供流化床生物气化器用于气化生物固体。 生物气化器包括反应器容器和用于在生物气化器的稳态操作期间以期望的进料速率将生物固体进料到反应器容器中的进料器。 在反应器容器底部的流化床具有与至少燃料供给速率成比例的横截面积，使得气体的表观速度在0.1m / s（0.33ft / s）至3的范围内 m / s（9.84ft / s）。 在气化生物固体的方法中，将生物固体进料到流化床反应器中。 将氧化剂气体施加到流化床反应器以产生0.1m / s（0.33ft / s）至3m / s（9.84ft / s）范围内的发生气体的表观速度。 在具有亚化学计量氧水平的氧缺乏环境中，将生物固体在流化床反应器内加热至900°F（482.2℃）至1700°F（926.7℃）之间的温度范围，由此 生物固体气化。

公开(公告)号：US20130195727A1

公开(公告)日：2013-08-01

申请号：US13361582

申请日：2012-01-30

申请人： Douglas R. Bull ,  Ross M. Patten ,  Paul Cairney ,  Gerald M. Cox ,  William P. Jepson

发明人： Douglas R. Bull ,  Ross M. Patten ,  Paul Cairney ,  Gerald M. Cox ,  William P. Jepson

IPC分类号： B01J8/18 ,  B23P17/00 ,  C07C5/02

CPC分类号： C10J3/466 ,  B01J8/1809 ,  B01J8/1827 ,  B01J2208/00893 ,  B01J2208/00902 ,  C02F11/10 ,  C02F11/12 ,  C02F11/121 ,  C10J3/482 ,  C10J3/84 ,  C10J2300/0909 ,  C10J2300/0916 ,  C10J2300/0923 ,  C10J2300/0956 ,  C10J2300/1643 ,  C10J2300/1807 ,  C10K1/026 ,  Y02P20/129 ,  Y02W10/40 ,  Y10T29/49

摘要： A fluidized bed biogasifier is provided for gasifying biosolids. The biogasifier includes a reactor vessel and a feeder for feeding biosolids into the reactor vessel at a desired feed rate during steady-state operation of the biogasifier. A fluidized bed in the base of the reactor vessel has a cross-sectional area that is proportional to at least the fuel feed rate such that the superficial velocity of gas is in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). In a method for gasifying biosolids, biosolids are fed into a fluidized bed reactor. Oxidant gases are applied to the fluidized bed reactor to produce a superficial velocity of producer gas in the range of 0.1 m/s (0.33 ft/s) to 3 m/s (9.84 ft/s). The biosolids are heated inside the fluidized bed reactor to a temperature range between 900° F. (482.2° C.) and 1700° F. (926.7° C.) in an oxygen-starved environment having a sub-stoichiometric oxygen level, whereby the biosolids are gasified.

摘要翻译： 提供流化床生物气化器用于气化生物固体。 生物气化器包括反应器容器和用于在生物气化器的稳态操作期间以期望的进料速率将生物固体进料到反应器容器中的进料器。 在反应器容器底部的流化床具有与至少燃料供给速率成比例的横截面积，使得气体的表观速度在0.1m / s（0.33ft / s）至3的范围内 m / s（9.84ft / s）。 在气化生物固体的方法中，将生物固体进料到流化床反应器中。 将氧化剂气体施加到流化床反应器以产生0.1m / s（0.33ft / s）至3m / s（9.84ft / s）范围内的发生气体的表观速度。 在具有亚化学计量氧水平的氧缺乏环境中，将生物固体在流化床反应器内加热至900°F（482.2℃）至1700°F（926.7℃）之间的温度范围，由此 生物固体气化。