CN201865710U - Coal chemical-looping combustion power generating device - Google Patents
Coal chemical-looping combustion power generating device Download PDFInfo
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- CN201865710U CN201865710U CN2010206334855U CN201020633485U CN201865710U CN 201865710 U CN201865710 U CN 201865710U CN 2010206334855 U CN2010206334855 U CN 2010206334855U CN 201020633485 U CN201020633485 U CN 201020633485U CN 201865710 U CN201865710 U CN 201865710U
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Abstract
Description
技术领域:Technical field:
本实用新型涉及一种煤化学链燃烧发电装置,用在发电需减少二氧化碳排放场合。The utility model relates to a coal chemical chain combustion power generation device, which is used in occasions where carbon dioxide emissions need to be reduced for power generation.
背景技术:Background technique:
全球气候变暖主要是由于以CO2为主的温室气体大量排放而导致地球温室效应的加剧而造成的。控制和减少CO2的排放量对于解决大气温室效应和全球变暖的影响具有重要作用。我国是CO2排放大国,排放量约占世界CO2排放总量的1/5,其中大部分CO2是由燃煤产生的。在未来相当长的时期内,我国以煤炭为主的能源格局不会改变,煤炭消耗量将持续增长,以化石燃料为主要的能源生产中,CO2的排放量约占人类各种活动所引起的CO2排放总量的70%以上,控制燃煤生产中CO2的排放对于解决大气温室效应和全球变暖具有显著的作用。而从燃煤锅炉的尾气中分离CO2能耗非常大。Global warming is mainly caused by the intensification of the earth's greenhouse effect due to the massive emission of greenhouse gases, mainly CO 2 . Controlling and reducing CO2 emissions plays an important role in addressing the effects of atmospheric greenhouse effect and global warming. China is a major CO 2 emitter, accounting for about 1/5 of the world's total CO 2 emissions, most of which are produced by coal combustion. For a long period of time in the future, China's coal-based energy pattern will not change, and coal consumption will continue to grow. In the production of energy mainly based on fossil fuels, CO2 emissions account for about Controlling CO2 emissions from coal-fired production plays a significant role in solving the atmospheric greenhouse effect and global warming . However, the separation of CO2 from the tail gas of coal-fired boilers is very energy-intensive.
有基于此,申请人作出本实用新型,旨在采用无火焰燃烧,用化学链燃烧方式分离出纯CO2,从而有效控制CO2排放。Based on this, the applicant made this utility model, which aims to separate pure CO 2 by using flameless combustion and chemical chain combustion, so as to effectively control CO 2 emissions.
实用新型内容:Utility model content:
针对上述所要解决的技术问题,本实用新型的第一方面目的是提供一种煤化学链燃烧发电装置,其特征在于:包括煤气化炉,煤气化炉与空分器相连,第一旋风分离器与煤气化炉循环连接,还原器与第一旋风分离器相连,第二旋风分离器与还原器循环连接,还原器内置有NiO,氧化器与还原器的出料口相连,第三旋风分离器与氧化器循环连接,还原器与氧化器的出料口相连,一级涡轮机、饱和器、二级涡轮机分别与压气器相连,一级涡轮机与第二旋风分离器相连,冷凝器与一级涡轮机相连,氧化器与饱和器相连,二级涡轮机与第三旋风分离器相连,发电机分别与一级涡轮机、二级涡轮机相连。In view of the technical problems to be solved above, the first aspect of the utility model is to provide a coal chemical looping combustion power generation device, which is characterized in that it includes a coal gasifier, the coal gasifier is connected with the air separator, and the first cyclone separator It is connected to the coal gasifier in circulation, the reducer is connected to the first cyclone separator, the second cyclone separator is connected to the reducer in circulation, the reducer is built with NiO, the oxidizer is connected to the outlet of the reducer, and the third cyclone separator It is connected to the oxidizer cycle, the reducer is connected to the outlet of the oxidizer, the first-stage turbine, the saturator, and the second-stage turbine are respectively connected to the compressor, the first-stage turbine is connected to the second cyclone separator, and the condenser is connected to the first-stage turbine. The oxidizer is connected with the saturator, the second-stage turbine is connected with the third cyclone separator, and the generator is connected with the first-stage turbine and the second-stage turbine respectively.
本实用新型的有益效果如下:本实用新型采用空气经空分器后与煤一起送入煤气化炉,煤在气化炉内气化为CO、CH4,送入还原器内,在还原器内与NiO反应生成高温高压纯CO2气体,在一级涡轮机中作功,带动发电机发电,从一级涡轮机出来的气体经冷凝器冷凝成纯CO2气体和水,纯CO2气体加以加收。在还原器内生成的Ni送回氧化器中,经压气器、饱和器压缩的空气同时送入氧化器,产生氧化反应将Ni氧化成NiO,从氧化器旋风分离器中出来的N2气送到二级涡轮机中作功,带动发电机发电。本实用新型为一种无火焰燃烧技术,用化学链燃烧方式分离出纯CO2,从而有效控制CO2排放。The beneficial effects of the utility model are as follows: the utility model adopts the air to be sent into the coal gasifier together with the coal after passing through the air separator, and the coal is gasified into CO and CH 4 in the gasifier, and then sent into the reducer. React with NiO inside to generate high-temperature and high-pressure pure CO2 gas, which works in the first-stage turbine to drive the generator to generate electricity. The gas from the first-stage turbine is condensed into pure CO2 gas and water through the condenser, and the pure CO2 gas is added receive. The Ni generated in the reducer is sent back to the oxidizer, and the air compressed by the compressor and the saturator is sent to the oxidizer at the same time, and an oxidation reaction occurs to oxidize Ni into NiO, and the N2 gas from the cyclone separator of the oxidizer is sent to Work in the secondary turbine to drive the generator to generate electricity. The utility model is a flameless combustion technology, which separates pure CO 2 through chemical chain combustion, thereby effectively controlling CO 2 emission.
下面结合附图1和具体实施例对本实用新型进一步的详细说明,以下实施例是对本实用新型的解释但本实用新型不局限于以下实施例。Below in conjunction with accompanying drawing 1 and specific embodiment, the utility model is further described in detail, and the following examples are explanations of the utility model, but the utility model is not limited to the following examples.
附图说明:Description of drawings:
图1为本实用新型的煤化学链燃烧发电装置的结构示意图。Fig. 1 is a structural schematic diagram of the coal chemical looping combustion power generation device of the present invention.
具体实施方式:Detailed ways:
如图1所示,本实用新型的煤化学链燃烧发电装置,包括煤气化炉1,煤气化炉1与空分器13相连,旋风分离器2与煤气化炉1循环连接,还原器3与旋风分离器2相连,旋风分离器4与还原器3循环连接,还原器3内置有NiO,氧化器12与还原器3的出料口相连,旋风分离器11与氧化器12循环连接,还原器3与氧化器12的出料口相连,一级涡轮机7、饱和器6、二级涡轮机10分别与压气器5相连,一级涡轮机7与旋风分离器4相连,冷凝器8与一级涡轮机7相连,氧化器12与饱和器6相连,二级涡轮机10与旋风分离器11相连,发电机9分别与一级涡轮机7、二级涡轮机10相连。As shown in Figure 1, the coal chemical chain combustion power generation device of the present utility model comprises a coal gasifier 1, the coal gasifier 1 is connected with the
结合图1所示,本实用新型的煤化学链燃烧发电工艺流程如下:As shown in Figure 1, the coal chemical chain combustion power generation process of the utility model is as follows:
1、空气经空分器13后与煤一起送入煤气化炉1,煤气化炉1与旋风分离器2组成循环流化床,煤在气化炉1内气化为CO、CH4,渣从气化炉1下部排出;1. After passing through the
2、煤气化炉1内生成的CO、CH4送入还原器3内,还原器3与旋风分离器4组成循环流化床,在还原器3内,CO、CH4与NiO反应生成高温高压纯CO2气体,反应方程式为:2. The CO and CH 4 generated in the coal gasifier 1 are sent to the reducer 3, and the reducer 3 and the cyclone separator 4 form a circulating fluidized bed. In the reducer 3, CO, CH 4 and NiO react to generate high temperature and high pressure Pure CO2 gas, the reaction equation is:
CO+CH4+NiO→CO2+H2O+Ni (1)CO+ CH4 +NiO→ CO2 + H2O +Ni (1)
3、在还原器3内反应生成的高温高压纯CO2气体,经旋风分离器4送入到一级涡轮机7中作功,带动发电机9发电,从一级涡轮机7出来的气体,经冷凝器8冷凝成纯CO2气体和水,纯CO2气体加以回收。3. The high-temperature and high-pressure pure CO2 gas generated by the reaction in the reducer 3 is sent to the first-stage turbine 7 through the cyclone separator 4 to do work, and drives the generator 9 to generate electricity. The gas coming out of the first-stage turbine 7 is condensed 8 is condensed into pure CO 2 gas and water, and the pure CO 2 gas is recovered.
4、在还原器3内生成的Ni被送至氧化器12中,经压气器5、饱和器6压缩后的空气同时送入氧化器12中,氧化器12与旋风分离器11组成循环流化床,产生氧化反应将Ni氧化成NiO,生成的NiO送至还原器3内循环使用。反应方程式为:4. The Ni generated in the reducer 3 is sent to the
Ni+O2→NiO (2)Ni+O 2 →NiO (2)
5、从旋风分离器11中出来的的N2气送到二级涡轮机10中作功,带动发电机9发电。5. The N2 gas coming out of the
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010206334855U CN201865710U (en) | 2010-11-26 | 2010-11-26 | Coal chemical-looping combustion power generating device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010206334855U CN201865710U (en) | 2010-11-26 | 2010-11-26 | Coal chemical-looping combustion power generating device |
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| CN201865710U true CN201865710U (en) | 2011-06-15 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102052102A (en) * | 2010-11-26 | 2011-05-11 | 绍兴文理学院 | Coal chemical chain combustion generating process and device |
| CN103946633A (en) * | 2011-09-20 | 2014-07-23 | Ifp新能源公司 | Chemical looping combustion method with removal of ash and fines in the reduction area, and a facility using such a method |
| US9692069B2 (en) | 2013-03-15 | 2017-06-27 | Ziet, Llc | Processes and systems for storing, distributing and dispatching energy on demand using and recycling carbon |
-
2010
- 2010-11-26 CN CN2010206334855U patent/CN201865710U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102052102A (en) * | 2010-11-26 | 2011-05-11 | 绍兴文理学院 | Coal chemical chain combustion generating process and device |
| CN103946633A (en) * | 2011-09-20 | 2014-07-23 | Ifp新能源公司 | Chemical looping combustion method with removal of ash and fines in the reduction area, and a facility using such a method |
| US9726369B2 (en) | 2011-09-20 | 2017-08-08 | Total Sa | Chemical-looping combustion method with ashes and fines removal in the reduction zone and plant using same |
| US9692069B2 (en) | 2013-03-15 | 2017-06-27 | Ziet, Llc | Processes and systems for storing, distributing and dispatching energy on demand using and recycling carbon |
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Granted publication date: 20110615 Termination date: 20131126 |