CN101251045B - Biomass energy circulating power generation process and power generation system thereof - Google Patents

Biomass energy circulating power generation process and power generation system thereof Download PDF

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CN101251045B
CN101251045B CN200810087169XA CN200810087169A CN101251045B CN 101251045 B CN101251045 B CN 101251045B CN 200810087169X A CN200810087169X A CN 200810087169XA CN 200810087169 A CN200810087169 A CN 200810087169A CN 101251045 B CN101251045 B CN 101251045B
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biomass
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黄家笙
林文彬
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/14Combined heat and power generation [CHP]
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/12Improving ICE efficiencies
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02TCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
    • Y02T10/00Road transport of goods or passengers
    • Y02T10/10Internal combustion engine [ICE] based vehicles
    • Y02T10/30Use of alternative fuels, e.g. biofuels

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Abstract

A biomass energy cycle power generation process is characterized by comprising the following steps: (1) gasifying the biomass raw material, converting the biomass raw material into combustible gas, and then sending the combustible gas into a gas internal combustion engine set to generate power after dedusting, decoking and purifying; (2) feeding biomass raw materials or ash residues generated in the gasification power generation process in the step 1 or a mixture of the biomass raw materials and the ash residues into a steam boiler to be combusted to generate superheated steam; introducing the exhaust waste heat of the gas internal combustion engine set in the step 1 into a waste heat boiler to generate superheated steam; (3) and (3) sending the superheated steam generated by the steam boiler and the waste heat boiler in the step (2) into a steam turbine generator unit together for power generation. The invention fully utilizes the heat energy and products generated in each processing link in the biomass energy gasification power generation process, circularly generates power, greatly improves the power generation efficiency, fully utilizes the waste and reduces the operation cost. The invention also discloses a power generation system for realizing the biomass energy circulating power generation process.

Description

一种生物质能循环发电工艺及其发电系统A biomass energy cycle power generation process and its power generation system

技术领域technical field

本发明涉及一种发电工艺及其发电系统,特别是涉及一种生物质能循环发电工艺及其发电系统。The invention relates to a power generation process and a power generation system thereof, in particular to a biomass energy cycle power generation process and a power generation system thereof.

背景技术Background technique

新能源技术作为二十一世纪世界经济发展中最具影响的技术之一,人类最终将依靠新能源产业的发展来解决全球的能源危机和环境污染问题,实现可持续发展。国家鼓励的可再生能源中,最大一块就是生物质能的发电和利用,我国拥有丰富的生物质能资源,据测算,我国理论生物质能资源为50亿吨左右。目前,可供利用开发的生物质能资源主要为生物质废弃物,包括农作物秸秆、谷壳、薪柴、工业有机废弃物和城市固体有机垃圾等。面对经济发展中如影随形的高消耗、高污染和资源环境约束问题,近年来,中国开始寻求经济增长模式的全面转变,走节约型发展道路。循环经济是一种以资源的高效利用和循环利用为核心,以″减量化、再利用、资源化″为原则,以低消耗、低排放、高效率为基本特征,符合可持续发展理念的经济增长模式,是对″大量生产、大量消费、大量废弃″的传统增长模式的根本变革。生物质能是一个重要的能源,预计到下世纪,世界能源消费的40%来自生物质能,我国有丰富的生物质能资源,我国农村能源的70%是生物质,仅农村秸杆每年总量达6亿多吨。随着经济的发展,人们生活水平的提高,环境保护意识的加强,对生物质能的合理、高效开发利用,必然愈来愈受到人们的重视。New energy technology is one of the most influential technologies in the world's economic development in the 21st century. Human beings will eventually rely on the development of new energy industries to solve the global energy crisis and environmental pollution problems and achieve sustainable development. Among the renewable energy encouraged by the state, the largest one is the power generation and utilization of biomass energy. my country has abundant biomass energy resources. According to estimates, my country's theoretical biomass energy resources are about 5 billion tons. At present, the available biomass energy resources are mainly biomass waste, including crop straw, chaff, firewood, industrial organic waste and municipal solid organic waste. Faced with the problems of high consumption, high pollution, and resource and environmental constraints that accompany economic development, in recent years, China has begun to seek a comprehensive transformation of the economic growth model and take the road of economical development. Circular economy is a kind of high-efficiency utilization and recycling of resources as the core, based on the principle of "reduction, reuse, and recycling", with low consumption, low emission, and high efficiency as the basic characteristics, in line with the concept of sustainable development The economic growth model is a fundamental change to the traditional growth model of "mass production, mass consumption, and mass waste". Biomass energy is an important energy source. It is estimated that by the next century, 40% of the world's energy consumption will come from biomass energy. my country has abundant biomass energy resources. 70% of my country's rural energy is biomass. The volume is more than 600 million tons. With the development of the economy, the improvement of people's living standards, the strengthening of environmental protection awareness, the reasonable and efficient development and utilization of biomass energy must be more and more valued by people.

目前,生物质气化发电的应用是洁净利用生物质能的有效方法之一,它可以在不产生污染的情况下把生物质能转化为电能,达到从低品位能源获取高品位能源的目的。特别是小型生物质气化发电工艺及发电系统,简单、灵活,比较容易推广应用。但中、大型生物质气化发电工艺及发电系统,发电量一般为≥2MW,在实际产业化过程中遇到很多现实问题,主要表现在如下几个方面:At present, the application of biomass gasification power generation is one of the effective methods for clean utilization of biomass energy. It can convert biomass energy into electric energy without generating pollution, and achieve the purpose of obtaining high-grade energy from low-grade energy. In particular, the small-scale biomass gasification power generation process and power generation system are simple, flexible, and relatively easy to popularize and apply. However, the medium and large biomass gasification power generation process and power generation system generally have a power generation ≥ 2MW, and encounter many practical problems in the actual industrialization process, mainly in the following aspects:

(1),系统利用效率偏低,一般只有15%左右,对这个问题曾经试图通过增加余热锅炉和蒸汽轮机发电来提高效率,但系统不稳定,达不到效果;(1) The utilization efficiency of the system is low, generally only about 15%. For this problem, attempts have been made to increase efficiency by adding waste heat boilers and steam turbines to generate electricity, but the system is unstable and the effect cannot be achieved;

(2),在气化、净化过程中产生大量的灰渣、污泥、有机污水、焦油等废弃物,这些废弃物含有很高的热量未被利用,虽然一部分可用来做肥料还田、也有一部分作为工业原料,如:保温材料、炼钢材料等,但大部分的废弃物没法利用,严重影响了电厂的正常运行,也给环境带来一定的危害;(2) A large amount of ash, sludge, organic sewage, tar and other wastes are produced in the process of gasification and purification. These wastes contain high heat and are not used. Although some of them can be used as fertilizers and returned to the field, some Some of them are used as industrial raw materials, such as: insulation materials, steelmaking materials, etc., but most of the waste cannot be used, which seriously affects the normal operation of the power plant and also brings certain harm to the environment;

(3),气体内燃机发电过程中效率也不高,一般为30%左右,大部分的热量从尾气和冷却水中散失掉了。(3), the efficiency of the gas internal combustion engine power generation process is not high, generally about 30%, and most of the heat is lost from the tail gas and cooling water.

综上,目前的中、大型生物质气化发电工艺及系统还存在很多问题没解决,电厂的运行费用过高,效率低下,如果不进一步提升效率,就很难商业化、产业化推广。To sum up, there are still many problems in the current medium and large-scale biomass gasification power generation process and system. The operating cost of the power plant is too high and the efficiency is low. If the efficiency is not further improved, it will be difficult to commercialize and promote industrialization.

发明内容Contents of the invention

本发明的目的是提供一种生物质能循环发电工艺及其发电系统,发电效率高,运行稳定,废弃物可被高效回收利用,环保无污染。The purpose of the present invention is to provide a biomass energy cycle power generation process and its power generation system, which have high power generation efficiency, stable operation, efficient recycling of waste, and are environmentally friendly and pollution-free.

本发明的技术方案可以通过以下的技术措施来实现,一种生物质能循环发电工艺,其特征在于包括如下步骤:The technical solution of the present invention can be realized by the following technical measures, a biomass energy cycle power generation process is characterized in that it comprises the following steps:

(1)将生物质原料进行气化,转换为可燃气体,然后经除尘、除焦净化后再送入气体内燃机组中发电;(1) The biomass raw material is gasified, converted into combustible gas, and then sent to the gas internal combustion unit for power generation after dedusting, decoking and purification;

(2)将生物质原料或步骤(1)所述的气化发电过程中产生的灰渣,或二者的混合物送入蒸汽锅炉中燃烧产生过热蒸汽,即在蒸汽锅炉中,可以仅燃烧气化发电过程中产生的灰渣,还可以燃烧生物质原料及灰渣的混合物,主要根据所要求的发电量来灵活控制;将步骤(1)所述的气体内燃机组的排气余热通入余热锅炉中产生过热蒸汽;所述的气化发电过程中产生的灰渣包括步骤(1)中所述的生物质原料气化后产生的干灰渣及所述的可燃气体净化后产生的湿灰渣;为了进一步利用发电过程中产生的余热,可以将步骤(1)中气化发电过程中产生的高温燃气余热先送入热交换器中产生汽水混合物,该汽水混合物再送入余热锅炉或蒸汽锅炉中,或者分别送到余热锅炉和蒸汽锅炉中,进一步产生过热蒸汽;(2) Send the biomass raw material or the ash generated in the gasification power generation process described in step (1), or the mixture of the two, into the steam boiler to burn to generate superheated steam, that is, in the steam boiler, only the gas can be burned The ash generated in the process of chemical power generation can also burn the mixture of biomass raw materials and ash, which is mainly flexibly controlled according to the required power generation; the exhaust waste heat of the gas internal combustion unit described in step (1) is passed into the waste heat Superheated steam is produced in the boiler; the ash produced in the gasification power generation process includes the dry ash produced after the gasification of the biomass raw material described in step (1) and the wet ash produced after the purification of the combustible gas slag; in order to further utilize the waste heat generated in the power generation process, the high-temperature gas waste heat generated in the gasification power generation process in step (1) can be sent to the heat exchanger to generate a steam-water mixture, and then the steam-water mixture is sent to the waste heat boiler or steam boiler or sent to waste heat boiler and steam boiler respectively to further generate superheated steam;

(3)将步骤(2)所述的蒸汽锅炉和余热锅炉产生的过热蒸汽一起送入汽轮发电机组中发电。(3) Send the steam boiler described in step (2) and the superheated steam produced by the waste heat boiler together into the turbogenerator unit to generate electricity.

本发明充分利用了生物质能气化发电过程中各处理环节所产生的热能和产物,循环发电,使发电效率大大提高、充分利用了废弃物,降低了运行成本。The invention makes full use of the heat energy and products generated in various processing links in the biomass energy gasification power generation process, and circulates power generation, so that the power generation efficiency is greatly improved, wastes are fully utilized, and operating costs are reduced.

本发明还可以作如下改进:将步骤(1)所述的气体内燃机组在循环冷却过程中产生的热水热能转换为电能,即可以将上述热水通过热交换设备与膨胀发电装置的介质进行热交换,从而让热交换后的介质蒸汽推动膨胀发电装置发电,如推动螺杆膨胀发电机组来产生电能,而热交换降温后的水继续用来冷却气体内燃机组,如此不断循环,达到充分利用热水余热的目的。The present invention can also be improved as follows: the heat energy of the hot water generated by the gas internal combustion unit described in step (1) in the cycle cooling process is converted into electric energy, that is, the above-mentioned hot water can be converted into electric energy through the medium of the heat exchange equipment and the expansion power generation device. Heat exchange, so that the medium steam after heat exchange drives the expansion power generation device to generate electricity, such as driving the screw expansion generator set to generate electricity, and the water after heat exchange and cooling continues to be used to cool the gas internal combustion set, so that the cycle is continuous to achieve full use of heat. The purpose of water waste heat.

本发明还可以进一步作如下改进:步骤(3)所述的汽轮发电机组在工作过程中也产生一些热水,如:汽轮机在循环冷却过程中产生的热水,本发明将这些热水热能也用来发电:将汽轮发电机组在工作过程中产生的热水的一部分或全部直接用来冷却气体内燃机组,然后将产生的热水进一步用来发电,如出来的热水可以通过热交换设备与膨胀发电装置的介质进行热交换,从而让热交换后的介质蒸汽推动膨胀发电装置发电,而汽轮机循环冷却系统中通过热交换降温后的水则继续下一循环冷却过程。The present invention can also be further improved as follows: the steam turbine generator set described in step (3) also produces some hot water in the working process, such as: the hot water produced by the steam turbine in the circulation cooling process, the present invention uses these hot water heat energy It is also used to generate electricity: part or all of the hot water generated by the turbo-generator unit is directly used to cool the gas internal combustion unit, and then the hot water generated is further used to generate electricity. For example, the hot water can be exchanged through heat The equipment exchanges heat with the medium of the expansion power generation device, so that the medium steam after heat exchange drives the expansion power generation device to generate electricity, and the water cooled by heat exchange in the steam turbine circulation cooling system continues the next cycle cooling process.

本发明利用气体发电和热水发电双循环发电系统可以带来双重经济效益:一方面可降低循环冷却系统的冷却水量,从而降低系统投资和水泵运行费用,降低自用电量,另一方面,可以增加余热发电量,提高系统效率。The invention utilizes gas power generation and hot water power generation double-cycle power generation system to bring double economic benefits: on the one hand, it can reduce the cooling water volume of the circulating cooling system, thereby reducing system investment and water pump operation costs, and reducing self-consumption electricity; on the other hand, it can increase Waste heat power generation, improve system efficiency.

本发明所述的生物质能循环发电工艺中,可以根据所要求的发电量选择是单独利用燃烧气化发电过程中产生的灰渣送入蒸汽锅炉发电,还是同时在蒸汽锅炉中燃烧生物质原料及灰渣的混合物发电。后者是可以将步骤(2)所述的生物质原料气化后产生的干灰渣及可燃气体净化后产生的湿灰渣先进行混合,然后再送入蒸汽锅炉中燃烧。In the biomass energy cycle power generation process described in the present invention, it can be selected according to the required power generation whether to use the ash generated in the combustion gasification power generation process alone to send it to the steam boiler for power generation, or to burn the biomass raw material in the steam boiler at the same time and ash mixture to generate electricity. In the latter, the dry ash produced after the gasification of the biomass raw material described in step (2) and the wet ash produced after the purification of the combustible gas can be mixed first, and then sent to the steam boiler for combustion.

用于实现上述生物质能循环发电工艺的一种生物质能发电系统,包括气化发电单元,所述的气化发电单元包括依次相连的气化炉、气体净化装置、气体内燃机组和循环冷却设备,其特征在于所述的发电系统还包括蒸汽发电单元,所述的蒸汽发电单元包括蒸汽锅炉、余热锅炉和汽轮发电机组,所述的气体内燃机组的尾气排放口连接到余热锅炉;所述的气体净化装置还连接有污水处理池,所述的气化炉上用于排放干灰渣的高温排灰阀和污水处理池的湿灰渣排放口共同连接到蒸汽锅炉的燃料进口;所述的余热锅炉与蒸汽锅炉并连后再和汽轮发电机组相连。所述的蒸汽发电单元的汽轮发电机组包括汽轮机和与其相连的发电机,所述的汽轮机上连接有汽轮机冷却水泵,该冷却水泵连接到所述循环冷却设备的冷水池;所述的循环冷却设备冷却汽轮机低压缸排气温度,降低低压缸排气压力,使得蒸汽在通过汽轮机时最大限度的释放能量做功转化为汽轮机旋转的机械能,从而用于驱动发电机发电。所述的汽轮机上连接有凝汽器,所述的凝汽器依次通过凝结水泵、除氧设备、给水泵和供水泵分别连接到余热锅炉和蒸汽锅炉,从而使汽轮机排出的蒸汽余热得到充分利用;其中,给水泵先经换热器再连接到余热锅炉。所述凝汽器的循环冷却水的进水管通过汽轮机冷却水泵与所述的冷水池相连,所述凝汽器的循环冷却水的回水管连接到气体内燃机组的冷却进水管,即冷却水泵将冷却水压入凝汽器中与作过功的过热蒸汽进行热交换,降低汽轮机末端排压,而吸收热量的循环水通过回水管被输送至气体内燃机组的冷却进水管,再用来冷却气体内燃机组。A biomass energy power generation system for realizing the above-mentioned biomass energy cycle power generation process, including a gasification power generation unit, and the gasification power generation unit includes a gasifier, a gas purification device, a gas internal combustion unit and a circulating cooling system connected in sequence The equipment is characterized in that the power generation system further includes a steam power generation unit, the steam power generation unit includes a steam boiler, a waste heat boiler and a steam turbine generator set, and the exhaust outlet of the gas internal combustion unit is connected to the waste heat boiler; The gas purification device is also connected with a sewage treatment tank, and the high-temperature ash discharge valve for discharging dry ash on the gasifier and the wet ash discharge port of the sewage treatment tank are jointly connected to the fuel inlet of the steam boiler; The waste heat boiler mentioned above is connected in parallel with the steam boiler and then connected with the steam turbine generator set. The turbogenerator set of the steam generating unit includes a steam turbine and a generator connected thereto, the steam turbine is connected with a steam turbine cooling water pump, and the cooling water pump is connected to the cold water pool of the circulating cooling equipment; the circulating cooling The equipment cools the exhaust temperature of the low-pressure cylinder of the steam turbine and reduces the exhaust pressure of the low-pressure cylinder, so that the steam can release energy to the maximum extent when it passes through the steam turbine and convert it into mechanical energy for the rotation of the steam turbine, which is used to drive the generator to generate electricity. The steam turbine is connected with a condenser, and the condenser is respectively connected to the waste heat boiler and the steam boiler through the condensate pump, the oxygen removal equipment, the feed water pump and the water supply pump, so that the waste heat of the steam discharged from the steam turbine can be fully utilized ; Among them, the feed water pump is first connected to the waste heat boiler through the heat exchanger. The inlet pipe of the circulating cooling water of the condenser is connected to the cold water pool through the steam turbine cooling water pump, and the return pipe of the circulating cooling water of the condenser is connected to the cooling inlet pipe of the gas internal combustion unit, that is, the cooling water pump will The cooling water is pressed into the condenser to exchange heat with the superheated steam that has done work, reducing the discharge pressure at the end of the steam turbine, and the circulating water that absorbs heat is sent to the cooling inlet pipe of the gas internal combustion unit through the return pipe, and then used to cool the gas internal combustion unit.

本发电系统在生物质能发电原理的基础上,将气体内燃机组的尾气余热进一步转换为电能,并对系统工作过程中产生的干、湿灰渣等废弃物进行再利用,即燃烧发电,环保节能,降低运行成本,发电效率大大提高。Based on the principle of biomass energy power generation, this power generation system further converts the exhaust heat of the gas internal combustion unit into electric energy, and reuses the dry and wet ash and other waste generated during the working process of the system, that is, combustion power generation, environmental protection Energy saving, lower operating costs, greatly improved power generation efficiency.

本发明所述的气化发电单元的气化燃气发电和所述的蒸汽发电单元的蒸汽发电,两部分组合成有机的整体,既可统一,又可独立,互不受限制,可以灵活运用。例如,当气体内燃机组检修时,可以在蒸汽锅炉中直接燃烧生物质原料来发电;或者,当燃烧灰渣的发电功率达不到要求时,也可以在蒸汽锅炉中填加一定量的生物质燃料作为补充,从而保证整个发电系统运行的稳定性。The gasification gas power generation of the gasification power generation unit of the present invention and the steam power generation of the steam power generation unit are combined into an organic whole, which can be unified or independent, not limited by each other, and can be used flexibly. For example, when the gas internal combustion unit is overhauled, the biomass raw material can be directly burned in the steam boiler to generate electricity; or, when the power generated by burning ash cannot meet the requirements, a certain amount of biomass can also be added to the steam boiler The fuel is used as a supplement to ensure the stability of the entire power generation system.

本发明可以作以下改进,所述的生物质发电系统还包括热水发电单元,其包括依次相连的热水池、热交换器和膨胀发电装置,所述的膨胀发电装置还依次连接有冷凝器和工质泵,所述的工质泵又与用于连接热水池的热交换器相连,该热交换器和冷凝器还连接到循环冷却设备的冷水池;所述的循环冷却设备的回水管与热水池相连。上述的热水发电单元将气体内燃机组在循环冷却过程中产生的热水热能转换为电能,充分利用了热水的余热,从而有效节约能源,提高了发电效率。The present invention can be improved as follows, the biomass power generation system also includes a hot water power generation unit, which includes a hot water pool, a heat exchanger and an expansion power generation device connected in sequence, and the expansion power generation device is also connected in turn with a condenser and Working fluid pump, described working fluid pump links to each other with the heat exchanger that is used to connect hot water pool again, and this heat exchanger and condenser are also connected to the cold water pool of circulating cooling equipment; The return pipe of described circulating cooling equipment is connected with A hot tub is attached. The above-mentioned hot water power generation unit converts the hot water heat energy generated by the gas internal combustion unit during the cycle cooling process into electric energy, fully utilizes the waste heat of the hot water, thereby effectively saving energy and improving power generation efficiency.

本发明所述的生物质能发电系统还可以包括干湿灰混合机,所述的气化炉的高温排灰阀和污水处理池的湿灰渣排放口均与所述的干湿灰混合机的入口相连,所述的干湿灰混合机的出口再连接到蒸汽锅炉。本发电系统中,干、湿灰混合后再燃烧,可以把湿灰中的焦油等污染物处理掉,既可排除湿灰,即污泥对环境的污染,又可以充分利用污泥的热量。The biomass power generation system of the present invention can also include a dry-wet ash mixer, and the high-temperature ash discharge valve of the gasifier and the wet ash discharge port of the sewage treatment tank are all connected with the dry-wet ash mixer. The inlet is connected, and the outlet of the dry-wet ash mixer is connected to the steam boiler. In this power generation system, the dry and wet ash are mixed and then burned to remove tar and other pollutants in the wet ash, which can not only eliminate the pollution of the wet ash, that is, sludge to the environment, but also make full use of the heat of the sludge.

与现有技术相比,本发明的优点是:Compared with prior art, the advantage of the present invention is:

(1).本发明所述的生物质能循环发电工艺及其发电系统,在传统的生物质能发电技术的基础上,综合创新,对生物质能采取集约化综合开发利用,增加了余热锅炉、蒸汽锅炉及汽轮发电机组,将气化发电与蒸汽发电相结合,在生物质能转化为电能的过程中,使资源得到高效、循环利用,节能环保,大大降低了运行成本;(1). The biomass energy cycle power generation process and its power generation system described in the present invention, on the basis of the traditional biomass energy power generation technology, comprehensively innovates, adopts intensive comprehensive development and utilization of biomass energy, and increases the waste heat boiler , steam boilers and turbogenerator sets, combining gasification power generation with steam power generation, in the process of converting biomass energy into electric energy, resources are efficiently and recycled, energy-saving and environmentally friendly, and greatly reduce operating costs;

(2).本发明还增加了生物质原料直接燃烧发电和热水发电环节,充分利用生物质能发电主系统发电过程中产生的热能及废弃产物,大大提高了发电的效率;(2). The present invention also increases the links of direct combustion of biomass raw materials for power generation and hot water power generation, making full use of the heat energy and waste products generated during the power generation process of the main system of biomass power generation, and greatly improving the efficiency of power generation;

(3).本发明所述的发电系统,气化燃气发电和蒸汽发电两部分组合成有机的整体,既可统一,又可独立,互不受限制,可以灵活运用,如:当部分气体内燃机组检修时,可以在蒸汽锅炉中直接掺入生物质原料和灰渣混合后燃烧发电,还可以根据现场条件在蒸汽锅炉中仅燃烧生物质原料或灰渣,从而保证整个发电系统运行的稳定性;本发电系统运行安全可靠,可广泛应用于中、大型生物质气化发电厂,具有极高的商业推广价值。(3). In the power generation system of the present invention, the two parts of gasification gas power generation and steam power generation are combined into an organic whole, which can be unified or independent, without mutual restriction, and can be used flexibly, such as: when part of the gas internal combustion engine During group maintenance, biomass raw materials and ash can be mixed directly into the steam boiler and then burned to generate electricity, or only biomass raw materials or ash can be burned in the steam boiler according to site conditions, so as to ensure the stability of the entire power generation system. ; The power generation system is safe and reliable in operation, can be widely used in medium and large biomass gasification power plants, and has extremely high commercial promotion value.

附图说明Description of drawings

图1是本发明实施例1的生物质能发电工艺组合流程框图;Fig. 1 is the flow block diagram of the combination process of biomass energy power generation process in embodiment 1 of the present invention;

图2是本发明实施例1的生物质能发电系统示意图;Fig. 2 is a schematic diagram of a biomass power generation system according to Embodiment 1 of the present invention;

图3是本发明实施例1的生物质能发电系统的气化发电单元示意图;3 is a schematic diagram of a gasification power generation unit of a biomass power generation system according to Embodiment 1 of the present invention;

图4是本发明实施例2的生物质能发电工艺组合流程框图;Fig. 4 is the flow block diagram of the combination process of biomass energy power generation process in embodiment 2 of the present invention;

图5是本发明实施例2的生物质能发电系统示意图;5 is a schematic diagram of a biomass power generation system according to Embodiment 2 of the present invention;

图6是本发明实施例2的的生物质能发电系统的气化发电单元示意图;6 is a schematic diagram of a gasification power generation unit of a biomass power generation system according to Embodiment 2 of the present invention;

图7是本发明实施例2的生物质能发电系统的蒸汽发电单元的蒸汽循环热力系统示意图。Fig. 7 is a schematic diagram of the steam cycle thermal system of the steam power generation unit of the biomass power generation system in Example 2 of the present invention.

具体实施方式Detailed ways

本发明的保护范围并不仅仅局限于以下的具体实施方式,其他人作出的非本质的改进,均属于本发明的保护范围之内。The scope of protection of the present invention is not limited to the following specific implementation methods, and non-essential improvements made by others all fall within the scope of protection of the present invention.

实施例1Example 1

本发明的实施例1如图1~3所示,本发明可以通过与大型米厂合作办电厂或在粮食生产基地办生物质发电厂来推广应用,可以根据当地的生物质资源来选择电厂的规模,一般为5MW和10MW两种规格。Embodiment 1 of the present invention is shown in Figures 1 to 3. The present invention can be popularized and applied by cooperating with large-scale rice factories to set up power plants or setting up biomass power plants in grain production bases. The power plant can be selected according to local biomass resources. The scale generally has two specifications of 5MW and 10MW.

本实施例的生物质能发电工艺,包括如下步骤:The biomass power generation process of the present embodiment comprises the following steps:

(1)将生物质原料进行处理,如将植物秸秆原料进行粉碎,而谷壳原料可以直接使用,然后将生物质原料进行气化,即把固体生物质转换为可燃气体,这些可燃气体的主要成份为CO、H2、CH4、CO2等,气化出来的燃气还包含一定的杂质,如灰分,焦炭,少量的焦油等;经除尘、除焦净化后再送入气体内燃机组中发电;(1) Treat biomass raw materials, such as crushing plant straw raw materials, and chaff raw materials can be used directly, and then gasify biomass raw materials, that is, convert solid biomass into combustible gases. The main source of these combustible gases The components are CO, H 2 , CH 4 , CO 2 , etc., and the gasified gas also contains certain impurities, such as ash, coke, a small amount of tar, etc.; after dedusting, decoking and purification, it is sent to the gas internal combustion unit for power generation;

(2)将步骤1的气化发电过程中的生物质原料气化后产生的干灰渣及可燃气体净化后产生的湿灰渣送入蒸汽锅炉21中燃烧,产生过热蒸汽;将步骤1的气体内燃机组13的排气余热通入余热锅炉9中产生过热蒸汽;(2) Send the dry ash produced after the gasification of the biomass raw material in the gasification power generation process of step 1 and the wet ash produced after the combustible gas purification into the steam boiler 21 to generate superheated steam; The exhaust waste heat of the gas internal combustion unit 13 is passed into the waste heat boiler 9 to generate superheated steam;

(3)将步骤2的蒸汽锅炉21和余热锅炉9产生的过热蒸汽一起并入主蒸汽母管,最后送入汽轮发电机组中来推动汽轮发电机组发电。(3) Merge the superheated steam generated by the steam boiler 21 and the waste heat boiler 9 in step 2 into the main steam main pipe, and finally send it into the turbo-generator set to drive the turbo-generator set to generate electricity.

实现上述生物质能发电工艺的发电系统,包括气化发电单元1、蒸汽发电单元2,气化发电单元1包括依次相连的气化炉11、气体净化装置12、气体内燃机组13、循环冷却水泵和冷水池7;气体内燃机组13与内燃机冷却水泵5的一端相连,内燃机冷却水泵5的另一端连接到冷水池7;蒸汽发电单元2包括蒸汽锅炉21、余热锅炉9和汽轮发电机组,汽轮发电机组包括汽轮机22和与其相连的发电机23,汽轮机22上与汽轮机冷却水泵6的一端相连,该冷却水泵的另一端连接到冷水池7;汽轮机22上还连接有凝汽器25,凝汽器25依次通过凝结水泵26、除氧设备27、给水泵28和供水泵30分别连接到余热锅炉9和蒸汽锅炉21,从汽轮机22排出的蒸汽余热得到充分利用。其中,给水泵28先经换热器29再连接到余热锅炉9。凝汽器25的循环冷却水的进水管通过汽轮机冷却水泵6与冷水池7相连。凝汽器25的循环冷却水的回水管还连接到气体内燃机组13的冷却进水管,大大节省了冷水池7的用水量。The power generation system for realizing the above-mentioned biomass energy power generation process includes a gasification power generation unit 1 and a steam power generation unit 2. The gasification power generation unit 1 includes a gasifier 11, a gas purification device 12, a gas internal combustion unit 13, and a circulating cooling water pump connected in sequence. and cold water pool 7; gas internal combustion unit 13 is connected to one end of internal combustion engine cooling water pump 5, and the other end of internal combustion engine cooling water pump 5 is connected to cold water pool 7; steam generating unit 2 includes steam boiler 21, waste heat boiler 9 and steam turbine generator set, steam The turbo-generator unit comprises a steam turbine 22 and a generator 23 connected thereto. The steam turbine 22 is connected to one end of the steam turbine cooling water pump 6, and the other end of the cooling water pump is connected to the cold water pool 7; the steam turbine 22 is also connected to a condenser 25, which The boiler 25 is connected to the waste heat boiler 9 and the steam boiler 21 respectively through the condensate pump 26 , deaeration equipment 27 , feed water pump 28 and feed water pump 30 , and the steam waste heat discharged from the steam turbine 22 is fully utilized. Wherein, the feed water pump 28 is first connected to the waste heat boiler 9 through the heat exchanger 29 . The inlet pipe of the circulating cooling water of the condenser 25 is connected with the cold water pool 7 through the steam turbine cooling water pump 6 . The return water pipe of the circulating cooling water of the condenser 25 is also connected to the cooling water inlet pipe of the gas internal combustion unit 13, which greatly saves the water consumption of the cold water pool 7.

气体净化装置12包括依次相连的一级文氏塔121、二级文氏塔122、三级喷淋塔123、四级喷淋塔124、污水分离器125、罗茨风机126、电除尘器127,电除尘器127经储气罐8连到气体内燃机组13;气体净化装置12还连接有污水处理池14,污水处理池14包括依次相连的喷淋塔污水循环池141、隔油池142、大污水循环池143、厌氧池144、好氧池145、斜沉池146和脱色池147,脱色池147再分别连至三、四级喷淋塔123、124的污水进水管,一级文氏塔121和二级文氏塔122的污水排水管连到隔油池142,三级喷淋塔123和四级喷淋塔124的污水排水管连到喷淋塔污水循环池141的进水口,经物理沉淀三、四级喷淋塔123、124出来的污水,去除污水中大颗粒沉淀物,沉淀后的水再被文氏塔利用,即喷淋塔污水循环池141的出水口再直接连到一级文氏塔121和二级文氏塔122的进水管。气化炉11包括原料仓111和气化炉炉体112,气化炉11与气体净化装置12之间还设有分离器17和热交换器18,热交换器18主要是用来吸收高温燃气的显热,热交换器18的下方还设有鼓风机的空气进口和空气出口,空气出口经鼓风机再连到气化炉11,用来提高气化反应的热效率。气化炉11的2个排灰口和分离器17的1个排灰口经其下方设有的用于排放干灰渣的高温排灰阀111a、112a、17a通过机械输送连接到蒸汽锅炉21的燃料进口;污水处理池14中的斜沉池146上的湿灰渣排放口经污泥浓缩池15和带式压滤机16也连接到蒸汽锅炉21的燃料进口。气体内燃机组13的尾气排放口连接到余热锅炉9,余热锅炉9与蒸汽锅炉21并连后再和汽轮发电机组的汽轮机22相连。The gas purification device 12 includes a first-stage Venturi tower 121, a second-stage Venturi tower 122, a third-stage spray tower 123, a fourth-stage spray tower 124, a sewage separator 125, a Roots fan 126, and an electrostatic precipitator 127 connected in sequence. , the electrostatic precipitator 127 is connected to the gas internal combustion unit 13 through the gas storage tank 8; the gas purification device 12 is also connected with a sewage treatment pool 14, and the sewage treatment pool 14 includes a spray tower sewage circulation pool 141, a grease trap 142, Large sewage circulation tank 143, anaerobic tank 144, aerobic tank 145, inclined settling tank 146 and decolorization tank 147, the decolorization tank 147 is connected to the sewage inlet pipes of the third and fourth spray towers 123 and 124 respectively, and the first-level civil The sewage drainage pipes of the Venturi tower 121 and the second-level Venturi tower 122 are connected to the grease trap 142, and the sewage drainage pipes of the third-level spray tower 123 and the fourth-level spray tower 124 are connected to the water inlet of the spray tower sewage circulation pool 141 , through the physical precipitation of the sewage from the third and fourth stage spray towers 123 and 124, the large particles of sediment in the sewage are removed, and the water after precipitation is used by the Venturi tower again, that is, the water outlet of the sewage circulation pool 141 of the spray tower is directly Connect to the water inlet pipe of the first-level Venturi tower 121 and the second-level Venturi tower 122. The gasification furnace 11 includes a raw material bin 111 and a gasification furnace body 112. A separator 17 and a heat exchanger 18 are also provided between the gasification furnace 11 and the gas purification device 12. The heat exchanger 18 is mainly used to absorb high-temperature gas Sensible heat, the air inlet and air outlet of the blower are provided under the heat exchanger 18, and the air outlet is connected to the gasifier 11 through the blower to improve the thermal efficiency of the gasification reaction. The two ash discharge ports of the gasifier 11 and one ash discharge port of the separator 17 are connected to the steam boiler 21 through the high-temperature ash discharge valves 111a, 112a, and 17a below which are used to discharge dry ash. The fuel inlet of the sewage treatment pond 14 on the inclined sedimentation tank 146 is also connected to the fuel inlet of the steam boiler 21 through the sludge thickening tank 15 and the belt filter press 16. The exhaust outlet of the gas internal combustion unit 13 is connected to the waste heat boiler 9, and the waste heat boiler 9 is connected in parallel with the steam boiler 21 and then connected to the steam turbine 22 of the turbogenerator set.

本实施例中,生物质原料包括农作物秸秆原料和谷壳原料两种,将本发电系统与原料处理系统3相连:秸秆原料由秸秆堆放场31经过秸秆粉碎机32和输送机33被输送到运行仓19,而谷壳由谷壳仓34直接被输送至运行仓19,原料由运行仓19进入气化炉炉体112中进行气化燃烧反应,而气化燃烧留下的干灰渣和可燃气体净化后产生的湿灰渣送入蒸汽锅炉21中直接燃烧发电,气体内燃机组13的排气余热通过余热锅炉9产生过热蒸汽。In this embodiment, biomass raw materials include crop straw raw materials and rice husk raw materials. The power generation system is connected to the raw material processing system 3: the straw raw materials are transported from the straw storage yard 31 through the straw pulverizer 32 and the conveyor 33 to the operation silo 19, while the chaff is directly transported from the chaff silo 34 to the operating silo 19, and the raw material enters the gasification furnace body 112 from the operating silo 19 for gasification and combustion reaction, while the dry ash and combustible slag left by the gasification combustion The wet ash generated after gas purification is sent to the steam boiler 21 for direct combustion to generate electricity, and the waste heat of the exhaust gas from the gas internal combustion unit 13 passes through the waste heat boiler 9 to generate superheated steam.

实施例2Example 2

本发明的实施例2如图4~7所示,与上一个实施例所不同的是,在生物质能发电的工艺中,在步骤2中,还将气化炉11出口的高温燃气余热先送入热交换器18中产生汽水混合物,该汽水混合物再送入余热锅炉9或蒸汽锅炉21中,或者分别送到余热锅炉9和蒸汽锅炉21中燃烧,进一步产生过热蒸汽,然后转入步骤3中推动汽轮发电机组发电;Embodiment 2 of the present invention is shown in Figures 4 to 7. The difference from the previous embodiment is that in the process of biomass power generation, in step 2, the waste heat of the high-temperature gas at the outlet of the gasifier 11 is first Send it into the heat exchanger 18 to generate a steam-water mixture, and then send the steam-water mixture into the waste heat boiler 9 or the steam boiler 21, or send it to the waste heat boiler 9 and the steam boiler 21 for combustion, further generate superheated steam, and then transfer to step 3 Promote the steam turbine generator set to generate electricity;

在步骤2中,将生物质原料气化后产生的干灰渣及可燃气体净化后产生的湿灰渣先进行混合,然后再送入蒸汽锅炉21中燃烧;In step 2, the dry ash produced after the gasification of the biomass raw material and the wet ash produced after the purification of the combustible gas are first mixed, and then sent to the steam boiler 21 for combustion;

在步骤2中,在必要时,还在蒸汽锅炉21中直接掺入生物质原料和灰渣混合后燃烧,产生过热蒸汽;In step 2, when necessary, the biomass raw material and ash are directly mixed in the steam boiler 21 and then burned to generate superheated steam;

将步骤1的气体内燃机组13在循环冷却过程中产生的热水热能转换为电能:热水经热水池43再通过热交换器42与膨胀发电装置的介质进行热交换,从而让热交换后的介质蒸汽推动螺杆膨胀发电机组来产生电能,而热交换降温后的水重新回到冷水池7,继续用来冷却气体内燃机组13,如此不断循环。Convert the hot water thermal energy generated by the gas internal combustion unit 13 in the cycle cooling process in step 1 into electric energy: the hot water passes through the hot water pool 43 and then passes through the heat exchanger 42 to exchange heat with the medium of the expansion power generation device, so that the heat exchanged The medium steam pushes the screw expansion generator set to generate electric energy, and the water after heat exchange and cooling returns to the cold water pool 7, and continues to be used to cool the gas internal combustion set 13, so that the cycle continues.

步骤3的汽轮发电机组的汽轮机22在循环冷却过程中产生热水,将这些热水热能也进行发电:将上述热水的一部分或全部直接用来冷却气体内燃机组13,然后将产生的热水进一步用来发电,热水经热水池43,并通过热交换器42与膨胀发电装置的介质进行热交换,从而让热交换后的介质蒸汽推动螺杆膨胀发电机组发电,而汽轮机循环冷却系统中通过热交换降温后的水重新回到冷水池7,如此不断循环。The steam turbine 22 of the turbo-generator set in step 3 produces hot water during the circulation cooling process, and the heat energy of the hot water is also used for power generation: a part or all of the above-mentioned hot water is directly used to cool the gas internal combustion unit 13, and then the generated heat is The water is further used to generate electricity. The hot water passes through the hot water pool 43 and exchanges heat with the medium of the expansion power generation device through the heat exchanger 42, so that the medium steam after the heat exchange drives the screw expansion power generation unit to generate electricity, and the steam turbine circulation cooling system The water cooled by the heat exchange returns to the cold water pool 7 again, and so continues to circulate.

另外,可将蒸汽锅炉21排污产生的低压蒸汽、汽封和轴封泄漏产生的低压蒸汽直接连接到热水池43进一步用来发电或供暧。In addition, the low-pressure steam generated by the blowdown of the steam boiler 21 and the low-pressure steam generated by the leakage of the steam seal and the shaft seal can be directly connected to the hot water pool 43 for further power generation or heating.

实现本实施例的生物质能发电工艺的发电系统,与上一个实施例所不同的是,热交换器18的下方设有进水口和出水口,进水口连接到给水泵28,出水口经供水泵30分别和余热锅炉9、蒸汽锅炉21的给水口相连,进一步产生过热蒸汽来推动汽轮发电机组发电,其中,供水泵30先经换热器29再连接到余热锅炉9。The power generation system for realizing the biomass power generation process of this embodiment is different from the previous embodiment in that a water inlet and a water outlet are provided under the heat exchanger 18, the water inlet is connected to the feed water pump 28, and the water outlet is connected to the water supply pump 28. The water pump 30 is respectively connected to the waste heat boiler 9 and the water supply port of the steam boiler 21 to further generate superheated steam to drive the turbogenerator to generate electricity. The water supply pump 30 is connected to the waste heat boiler 9 through the heat exchanger 29 first.

发电系统还包括干湿灰混合机10,原料仓111、气化炉炉体112和分离器17下面的高温排灰阀111a、112a、17a均与干湿灰混合机10的入口相连,污水处理池14的湿灰渣排放口也经污泥浓缩池15和带式压滤机16连接到干湿灰混合机10的入口,干湿灰混合机10的出口再连接到蒸汽锅炉21。The power generation system also includes a dry-wet ash mixer 10, and the high-temperature ash discharge valves 111a, 112a, and 17a below the raw material bin 111, the gasifier body 112 and the separator 17 are all connected to the inlet of the dry-wet ash mixer 10, and the sewage treatment The wet ash discharge port of the pool 14 is also connected to the inlet of the wet and dry ash mixer 10 through the sludge thickening tank 15 and the belt filter press 16, and the outlet of the wet and dry ash mixer 10 is connected to the steam boiler 21 again.

气化发电系统还包括热水发电单元4,其包括依次相连的热水池43、循环热水泵48、过滤器49、热交换器42和膨胀发电装置,膨胀发电装置为螺杆膨胀发电机组,包括螺杆膨胀动力机44和发电机45,螺杆膨胀动力机44上还依次连接有冷凝器47和工质泵46,工质泵46又与热交换器42相连,热交换器42和冷凝器47还分别连接到冷水池7;气体内燃机组13循环冷却后的回水管与热水池43相连,上述的热水发电单元4将气体内燃机组13在循环冷却过程中产生的热水热能转换为电能。The gasification power generation system also includes a hot water power generation unit 4, which includes a hot water pool 43 connected in sequence, a circulating hot water pump 48, a filter 49, a heat exchanger 42 and an expansion power generation device. The expansion power generation device is a screw expansion power generation unit, including a screw Expansion power machine 44 and generator 45, and screw expansion power machine 44 is also connected with condenser 47 and working medium pump 46 successively, and working medium pump 46 links to each other with heat exchanger 42 again, and heat exchanger 42 and condenser 47 are also connected to respectively The cold water pool 7; the return pipe after the circulation cooling of the gas internal combustion unit 13 is connected to the hot water pool 43, and the above-mentioned hot water power generation unit 4 converts the hot water heat energy generated by the gas internal combustion unit 13 during the circulation cooling process into electric energy.

蒸汽锅炉21和余热锅炉9通过主蒸汽母管与汽轮机22相连,利用过热蒸汽来推动汽轮发电机组发电,汽轮机22还通过汽轮机冷却水泵6与冷水池7相连;汽轮机22的凝汽器25依次经凝结水泵26、除氧设备27、给水泵28连接到热交换器18的进水口。凝汽器25的循环冷却水的进水管通过汽轮机冷却水泵6与冷水池7相连,凝汽器25的循环冷却水的回水管连接到气体内燃机组13的冷却进水管,大大节省了冷水池7的用水量。The steam boiler 21 and the waste heat boiler 9 are connected to the steam turbine 22 through the main steam main pipe, and the superheated steam is used to drive the steam turbine generator set to generate electricity. The steam turbine 22 is also connected to the cold water pool 7 through the steam turbine cooling water pump 6; the condenser 25 of the steam turbine 22 is sequentially It is connected to the water inlet of the heat exchanger 18 via a condensate pump 26 , deaeration equipment 27 and a feed water pump 28 . The water inlet pipe of the circulating cooling water of the condenser 25 is connected to the cold water pool 7 through the steam turbine cooling water pump 6, and the return water pipe of the circulating cooling water of the condenser 25 is connected to the cooling water inlet pipe of the gas internal combustion unit 13, which greatly saves the cooling water pool 7 of water consumption.

热水发电单元4是采用热水和低沸点介质进行热交换,使介质蒸发后推动螺杆膨胀动力机44进行发电的技术,螺杆膨胀动力机44适用于蒸汽、汽水混合物、热水、被污染热源的各种介质。热水发电单元4的热水循环过程为:热水池43的热水进入热交换器42,与介质发生热交换后变成冷水,回到冷水池7,冷却汽轮发电机组的凝汽器25、螺杆膨胀动力机44的冷凝器47,然后再通过凝汽器25循环冷却后的回水管连接到气体内燃机组13的冷却进水管,冷却气体内燃机组13,产生的热水重新回到热水池43,继续下一循环。The hot water power generation unit 4 uses hot water and low-boiling medium for heat exchange, and drives the screw expansion power machine 44 to generate electricity after the medium evaporates. The screw expansion power machine 44 is suitable for steam, steam-water mixture, hot water, and polluted heat sources. medium. The hot water circulation process of the hot water power generation unit 4 is as follows: the hot water in the hot water pool 43 enters the heat exchanger 42, exchanges heat with the medium, turns into cold water, returns to the cold water pool 7, and cools the condenser 25 of the turbogenerator set , the condenser 47 of the screw expansion power machine 44, and then the return water pipe after cooling through the condenser 25 circulation is connected to the cooling water inlet pipe of the gas internal combustion unit 13, the gas internal combustion unit 13 is cooled, and the hot water produced returns to the hot water pool 43 , continue to the next cycle.

热水发电单元的介质循环过程为:介质通过工质泵46进入热交换器42,与热水发生热交换后,变成蒸汽推动螺杆膨胀发电机组发电,然后再通过冷凝器47冷凝,继续下一循环。上述的介质为低沸点的液体,一般为低于水的沸点,可以是氨水等介质。The medium circulation process of the hot water power generation unit is as follows: the medium enters the heat exchanger 42 through the working medium pump 46, and after heat exchange with the hot water, it becomes steam to drive the screw expansion generator set to generate electricity, and then condenses through the condenser 47, and continues to one cycle. The above-mentioned medium is a liquid with a low boiling point, generally lower than the boiling point of water, and may be a medium such as ammonia water.

蒸汽锅炉21还可以通过连续排污母管和定期排污母管分别与连续排污扩容器221和定期排污扩容器222相连,连续排污扩容器221还连接到低压蒸汽母管,低压蒸汽母管再连接到热水池43,使汽轮机在工作过程中产生的低温低压蒸汽的热量的得到充分利用。汽轮机22还可以连接有锅炉补水系统20,适用于蒸汽发电单元2缺水的情况,锅炉补水系统20包括工业水箱201和和工业水泵202,工业水箱201经工业水泵202连接到化学水处理系统,对水进行化学处理,处理后的软水连接到除盐水母管,与凝结水泵26相连的汽封加热器253连接到凝结水疏水母管,凝结水疏水母管通过疏水泵连接到疏水箱223。上述的除盐水母管和凝结水疏水母管共同连接到除氧设备27,除氧设备27包括除氧器271和与其相连的除氧水箱272,除氧水箱272经给水泵28连接到热交换器18。The steam boiler 21 can also be connected to the continuous sewage expansion vessel 221 and the regular sewage expansion vessel 222 respectively through the continuous sewage discharge main pipe and the regular sewage discharge main pipe. The continuous sewage discharge expansion vessel 221 is also connected to the low pressure steam main pipe, and the low pressure steam main pipe is then connected to The hot water pool 43 makes full use of the heat of the low-temperature and low-pressure steam produced by the steam turbine in the working process. The steam turbine 22 can also be connected with a boiler water supply system 20, which is applicable to the situation of water shortage of the steam generating unit 2. The boiler water supply system 20 includes an industrial water tank 201 and an industrial water pump 202. The industrial water tank 201 is connected to the chemical water treatment system through the industrial water pump 202. The water is chemically treated, the treated soft water is connected to the desalinated main pipe, the steam seal heater 253 connected to the condensate pump 26 is connected to the condensate drain main pipe, and the condensate drain main pipe is connected to the drain tank 223 through the drain pump. The above-mentioned desalinated water main pipe and condensed water hydrophobic main pipe are jointly connected to the deaeration equipment 27. The deaeration equipment 27 includes a deaeration device 271 and a deaeration water tank 272 connected thereto. The deaeration water tank 272 is connected to the heat exchange via a feed water pump 28 Device 18.

上述的实施例中,余热锅炉和蒸汽锅炉还可以串联组合后再连接到汽轮发电机组发电,二者串连的顺序可以任意设定。热水池的热水还可以用来冬季采暖,如把热水送到采暖点加热器,然后回到冷水池。此外,蒸汽锅炉燃烧后的尾气和余热锅炉排出的尾气余热有两种方法进一步利用:(1)作为干燥生物质原料和湿灰渣的热源;(2)经热水池的水吸热后排出。还可以将蒸汽锅炉燃烧后剩下的白灰进一步提炼成二氧化硅或加工肥料,如秸秆灰可以做钾肥,本发电系统最终的白灰含量已低于5%。还可以将生物质原料气化后产生的多余黑灰,即灰渣作进一步利用。上述的生物质原料还可以包括薪柴、工业有机废弃物等。In the above-mentioned embodiments, the waste heat boiler and the steam boiler can also be combined in series and then connected to the turbogenerator to generate electricity, and the sequence of the two in series can be set arbitrarily. The hot water in the hot water pool can also be used for heating in winter, as sending hot water to the heating point heater, and then returning to the cold water pool. In addition, there are two ways to further use the waste heat of the tail gas after the combustion of the steam boiler and the tail gas exhausted by the waste heat boiler: (1) as a heat source for drying biomass raw materials and wet ash; (2) after being discharged through the water in the hot water pool. It is also possible to further refine the lime ash left after the steam boiler is burned into silicon dioxide or process fertilizer, such as straw ash can be used as potash fertilizer, and the final lime content of this power generation system is lower than 5%. The excess black ash produced after the gasification of biomass raw materials, that is, ash residue, can also be further utilized. The aforementioned biomass raw materials may also include firewood, industrial organic waste, and the like.

上述的实施例中,当必要时,如部分气体内燃机组检修时,可以在蒸汽锅炉中直接掺入生物质原料和灰渣混合后燃烧发电,从而保证整个发电系统运行的稳定性。同理,在蒸汽锅炉中还可以仅燃烧灰渣,或仅燃烧生物质原料,主要根据所要求的发电量来灵活控制。In the above-mentioned embodiments, when necessary, such as when some gas internal combustion units are overhauled, the steam boiler can be directly mixed with biomass raw materials and ash to generate electricity, so as to ensure the stability of the entire power generation system. In the same way, only ash or biomass raw materials can be burned in the steam boiler, which is flexibly controlled mainly according to the required power generation.

Claims (7)

1. a biomass energy circulation electrification technique as well as is characterized in that comprising the steps:
(1) biomass material is gasified, be converted to inflammable gas, after dedusting, decoking purify, send into generating in the gas internal combustion unit (13) then again;
(2) with the lime-ash that produces in biomass material or the described gasifying electricity generation process of step (1), or the mixture of the two is sent into, and burning produces superheated vapor in the steam boiler (21); The exhaust heat of step (1) described gas internal combustion unit (13) is fed generation superheated vapor in the exhaust heat boiler (9); The lime-ash that produces in the described gasifying electricity generation process comprises that dry ash slag and described inflammable gas that the biomass material gasification back described in the step (1) produces purify the wet lime-ash that the back produces; The high-temperature fuel gas waste heat that produces in the gasifying electricity generation process in the described step (1) is sent into generation steam water interface in the heat exchanger (18) earlier, and this steam water interface is delivered to respectively in exhaust heat boiler (9) and the steam boiler (21) again, further produces superheated vapor;
(3) superheated vapor that the described steam boiler of step (2) (21) and exhaust heat boiler (9) are produced is sent in the Turbo-generator Set together and is generated electricity.
2. a kind of biomass energy circulation electrification technique as well as according to claim 1, it is characterized in that the hot water heat energy that step (1) described gas internal combustion unit (13) produces in the circulation cooling procedure is converted to electric energy: the medium of above-mentioned hot water by heat-exchange apparatus and expansion power generation device carried out heat exchange, thereby allow the medium steam after the heat exchange promote the generating of expansion power generation device, and the water after the heat exchange cooling continue to be used for cooled gas internal combustion unit (13).
3. a kind of biomass energy circulation electrification technique as well as according to claim 2, part or all that it is characterized in that hot water that Turbo-generator Set is produced in the course of the work directly is used for cooled gas internal combustion unit (13), then the hot water that the comes out medium by heat-exchange apparatus and expansion power generation device is carried out heat exchange, thereby allow the medium steam after the heat exchange promote the generating of expansion power generation device, the water after the heat exchange cooling then continues next circulation cooling procedure.
4. a kind of biomass energy circulation electrification technique as well as according to claim 3, it is characterized in that dry ash slag that will step (2) described biomass material gasification back produces and inflammable gas purify the wet lime-ash that the back produces and mix earlier, and then send into burning in the steam boiler (21).
5. biomass power generation system that is used for the described biomass energy circulation electrification technique as well as of claim 1, comprise gasifying electricity generation unit (1), described gasifying electricity generation unit (1) comprises the gasification oven (11) that links to each other successively, gas cleaning plant (12), gas internal combustion unit (13) and circulation cooling equipment, it is characterized in that described power generation system also comprises steam electric power unit (2), described steam electric power unit (2) comprises steam boiler (21), exhaust heat boiler (9) and Turbo-generator Set, the exhaust port of described gas internal combustion unit (13) is connected to exhaust heat boiler (9), and described gas cleaning plant (12) also is connected with treatment tank (14); The wet lime-ash floss hole that is used to discharge the high temperature Ash valves of dry ash slag and treatment tank (14) on the described gasification oven (11) is connected to the fuel inlet of steam boiler (21) jointly; Described exhaust heat boiler (9) links to each other with Turbo-generator Set with steam boiler (21) and Lian Houzai; The Turbo-generator Set of described steam electric power unit (2) comprises steam turbine (22) and coupled generator (23), be connected with steam turbine cooling waterpump (6) on the described steam turbine (22), this cooling waterpump is connected to the water cooling pond (7) of described circulation cooling equipment; Also be connected with vapour condenser (25) on the described steam turbine (22), described vapour condenser (25) is connected respectively to exhaust heat boiler (9) and steam boiler (21) by condensate pump (26), deaeration plant (27), feed water pump (28) and raw water service pump (30) successively; The intake pipe of the recirculated cooling water of described vapour condenser (25) links to each other with described water cooling pond (7) by steam turbine cooling waterpump (6), and the return pipe of the recirculated cooling water of described vapour condenser (25) is connected to the cooling intake pipe of gas internal combustion unit (13).
6. biomass power generation according to claim 5 system, it is characterized in that also being provided with heat exchanger (18) between described gasification oven (11) and the gas cleaning plant (12), the below of heat exchanger (18) is provided with water intake and water outlet, the water intake of heat exchanger (18) is connected to described feed water pump (28), and water outlet links to each other with the admission port of exhaust heat boiler (9), steam boiler (21) respectively through raw water service pump (30).
7. according to claim 5 or 6 described biomass power generation systems, it is characterized in that described power generation system also comprises hot water generator unit (4), it comprises hot-tub (43), heat exchanger (42) and the expansion power generation device that links to each other successively, described expansion power generation device also is connected with condenser (47) and working medium pump (46) in turn, described working medium pump (46) links to each other with the heat exchanger that is used to be connected hot-tub (43) (42) again, and this is used to connect the heat exchanger (42) of hot-tub and the water cooling pond (7) that condenser (47) is also connected to the circulation cooling equipment; The return pipe of described circulation cooling equipment links to each other with hot-tub (43).
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101892877A (en) * 2010-07-20 2010-11-24 华北电力大学(保定) A Hybrid Power Generation System with Renewable Energy Assisting Coal Combustion
CN101906996A (en) * 2010-07-20 2010-12-08 华北电力大学(保定) A coal-fired combined power generation system assisted by biomass and solar energy
CN102080821A (en) * 2010-11-17 2011-06-01 华北电力大学(保定) Heater system for renewable energy auxiliary coal

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CN102699007A (en) * 2012-05-31 2012-10-03 郭涵 Method for treating household garbage and realizing co-production by using lime kiln
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1121155A (en) * 1994-10-20 1996-04-24 机械工业部上海发电设备成套设计研究所 Forced-circulation diesel oil engine afterheat boiler electricity-generating system
CN1258712A (en) * 1998-12-30 2000-07-05 中国科学院广州能源研究所 Biomass gasifying and purifying circular fluid-bed system

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1121155A (en) * 1994-10-20 1996-04-24 机械工业部上海发电设备成套设计研究所 Forced-circulation diesel oil engine afterheat boiler electricity-generating system
CN1258712A (en) * 1998-12-30 2000-07-05 中国科学院广州能源研究所 Biomass gasifying and purifying circular fluid-bed system

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101892877A (en) * 2010-07-20 2010-11-24 华北电力大学(保定) A Hybrid Power Generation System with Renewable Energy Assisting Coal Combustion
CN101906996A (en) * 2010-07-20 2010-12-08 华北电力大学(保定) A coal-fired combined power generation system assisted by biomass and solar energy
CN102080821A (en) * 2010-11-17 2011-06-01 华北电力大学(保定) Heater system for renewable energy auxiliary coal

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