CN203960020U - A kind of system of utilizing the dry municipal sludge of surplus heat of power plant coupled solar - Google Patents
A kind of system of utilizing the dry municipal sludge of surplus heat of power plant coupled solar Download PDFInfo
- Publication number
- CN203960020U CN203960020U CN201420265838.9U CN201420265838U CN203960020U CN 203960020 U CN203960020 U CN 203960020U CN 201420265838 U CN201420265838 U CN 201420265838U CN 203960020 U CN203960020 U CN 203960020U
- Authority
- CN
- China
- Prior art keywords
- sludge
- air
- water
- heat
- mud
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/30—Wastewater or sewage treatment systems using renewable energies
- Y02W10/37—Wastewater or sewage treatment systems using renewable energies using solar energy
Landscapes
- Treatment Of Sludge (AREA)
- Drying Of Solid Materials (AREA)
Abstract
一种利用电站余热耦合太阳能干燥城市污泥的系统,含:汽水流程:一凝汽器,水道进口接冷却塔(10)循环水、出口一路经空气-水热交换器(9)、另外一路经污泥加热器(1),两者最后都送回冷却塔(10)中;凝汽器热汽源来自汽轮机(4)排出来的乏汽;空气流程:一鼓风机(8),将空气依次送到热交换器9、太阳能集热板(6)和流化床干燥器(2),最后经过除尘器5排入大气;污泥流程:经粉碎机粉碎的污泥进入污泥加热器1后落入流化床式干燥器2最后由输送皮带输送到料仓3。本系统充分利用了电厂内的余热以及厂区内的太阳能,提高了电厂的热经济性,通过干燥技术处理污泥,使其达到稳定化、无害化、减量化,为进一步资源化利用打下基础,具有重要的现实意义。
A system for drying urban sludge using waste heat from a power station coupled with solar energy, including: steam-water flow: a condenser, the inlet of the water channel is connected to the circulating water of the cooling tower (10), the outlet of one channel passes through the air-water heat exchanger (9), and the other channel After the sludge heater (1), both are sent back to the cooling tower (10) at last; the hot steam source of the condenser comes from the exhaust steam discharged from the steam turbine (4); the air flow: a blower (8), the air Sent to heat exchanger 9, solar heat collector plate (6) and fluidized bed dryer (2) in turn, and finally discharged into the atmosphere through dust collector 5; sludge process: the sludge pulverized by the pulverizer enters the sludge heater 1 and then fall into the fluidized bed dryer 2 and finally transported to the silo 3 by the conveyor belt. This system makes full use of the waste heat in the power plant and the solar energy in the plant area, improves the thermal economy of the power plant, and treats the sludge through drying technology to achieve stabilization, harmlessness, and reduction, laying a solid foundation for further resource utilization. foundation, has important practical significance.
Description
技术领域technical field
本实用新型涉及一种利用电站余热耦合太阳能干燥城市污泥的系统。The utility model relates to a system for drying urban sludge by utilizing waste heat of a power station coupled with solar energy.
背景技术Background technique
随着我国社会经济的发展和城市人口的增加,环境污染日益严重,而人们对生存环境的保护和改善意识不断加强必然促使越来越多的废水需要处理。我国2010年污水排放量将达到4.40×1010m3/d,预计2020年污水排放量将达到5.36×1010m3/d,因此每年至少产生500万吨污泥。而国内外实践表明,经传统的浓缩和脱水工艺处理后,污泥的含水率不可能达到60%以下,经机械脱水,污泥含水率为75%左右。要达到对污泥的进一步脱水,比较经济的方法是引入化工操作中常用的干燥技术,而这些干燥技术无疑将会耗费巨大的能源。With the development of my country's social economy and the increase of urban population, environmental pollution is becoming more and more serious, and people's awareness of protecting and improving the living environment will inevitably lead to more and more wastewater treatment. China's sewage discharge in 2010 will reach 4.40×10 10 m 3 /d, and it is estimated that the sewage discharge in 2020 will reach 5.36×10 10 m 3 /d, so at least 5 million tons of sludge will be produced every year. However, practice at home and abroad shows that after the traditional concentration and dehydration process, the water content of the sludge cannot reach below 60%, and after mechanical dehydration, the water content of the sludge is about 75%. To achieve further dehydration of sludge, a more economical method is to introduce drying techniques commonly used in chemical operations, and these drying techniques will undoubtedly consume huge energy.
另一方面,目前大型火力发电机组节能减排是国家重要政策之一。电厂循环水温度较低,所含能量品质较差,而一直以来,其余热回收途径较少,因此开发电站循环水余热回收利用技术,开创了电站节能减排的新途径,对提高电厂热经济性,增加电站经济效益具有重要意义。同时结合太阳能这一新能源的综合利用,会大大提高循环水的能量品质,其回收余热的利用效率也会大大增加。一般机械脱水后的污泥含水率在80%左右,其中自由水分比例较大,为污泥低温干燥创造了条件。On the other hand, energy saving and emission reduction of large thermal power generating units is one of the important national policies. The temperature of circulating water in power plants is low, and the quality of energy contained in them is poor, and there have always been few ways to recover the remaining heat. Therefore, the development of waste heat recovery and utilization technology for circulating water in power plants has created a new way for power plants to save energy and reduce emissions, which is very important for improving the thermal economy of power plants. It is of great significance to increase the economic benefits of power stations. At the same time, combined with the comprehensive utilization of solar energy, a new energy source, the energy quality of circulating water will be greatly improved, and the utilization efficiency of waste heat recovery will also be greatly increased. Generally, the moisture content of sludge after mechanical dehydration is about 80%, and the proportion of free moisture is relatively large, which creates conditions for low-temperature drying of sludge.
利用电厂循环水余热的城市污泥干燥技术的原理是用具有一定温度的循环水加热污泥和空气,再由热空气干燥被加热的污泥,从而达到污泥干燥的目的。空气被循环水初步加热后,再被布置在热交换器出口的太阳能集热板加热,温度达到65℃。这时将空气送往流化床式干燥器中干燥污泥能取得不错的效果,通过干燥技术处理污泥,使其达到稳定化、无害化、减量化,为进一步资源化利用打下基础,具有重要的现实意义。The principle of municipal sludge drying technology using the waste heat of circulating water in power plants is to heat sludge and air with circulating water at a certain temperature, and then dry the heated sludge by hot air, so as to achieve the purpose of sludge drying. After the air is preliminarily heated by the circulating water, it is then heated by the solar collector panels arranged at the outlet of the heat exchanger, and the temperature reaches 65°C. At this time, sending the air to the fluidized bed dryer to dry the sludge can achieve good results, and the sludge can be treated by drying technology to achieve stabilization, harmlessness and reduction, laying the foundation for further resource utilization , has important practical significance.
实用新型内容Utility model content
本实用新型所要解决的技术问题,就是提供一种利用电站循环水耦合太阳能干燥城市污泥的系统,提高燃煤电站热经济性,为城市污泥下一步进行资源化利用(掺混燃烧、农业肥料、土壤改良剂等)打下基础。The technical problem to be solved by the utility model is to provide a system that utilizes power station circulating water to couple solar energy to dry urban sludge, improve the thermal economy of coal-fired power stations, and perform resource utilization for urban sludge in the next step (mixing combustion, agricultural fertilizers, soil amendments, etc.) to lay the foundation.
解决上述技术问题,本实用新型所采用的技术方案如下:To solve the problems of the technologies described above, the technical solution adopted in the utility model is as follows:
一种利用电站循环水耦合太阳能干燥城市污泥的系统,其特征是包括汽水、空气和污泥三流程;所述的汽水流程含:一凝汽器,其水道进口接电站冷却塔10输出的循环水、水道出口分为两路:一路经空气-水热交换器9、另外一路经污泥加热器1,两者最后都接入电厂原来的循环水循环管道中送回冷却塔10中;凝汽器热汽源来自汽轮机4排出来的乏汽;所述的空气流程含:一鼓风机8,将空气经管道依次送到热交换器9和太阳能集热板6加热后进入流化床干燥器2加热污泥,最后经过除尘器5,达到排放标准后通过烟囱排入大气;所述的污泥流程含:经粉碎机粉碎的污泥进入污泥加热器1后落入流化床式干燥器2最后由输送皮带输送到料仓3。A system for drying municipal sludge using circulating water coupled with solar energy in a power station is characterized in that it includes three processes of steam water, air and sludge; Circulating water and the outlet of the water channel are divided into two paths: one path passes through the air-water heat exchanger 9, and the other path passes through the sludge heater 1, both of which are finally connected to the original circulating water circulation pipeline of the power plant and sent back to the cooling tower 10; The hot steam source of the boiler comes from the exhaust steam discharged from the steam turbine 4; the air process includes: a blower 8, which sends the air through the pipeline to the heat exchanger 9 and the solar heat collector 6 to be heated and then enters the fluidized bed dryer 2 Heating the sludge, and finally passing through the dust collector 5, and discharging it into the atmosphere through the chimney after reaching the discharge standard; the sludge process includes: the sludge pulverized by the pulverizer enters the sludge heater 1 and then falls into the fluidized bed drying The container 2 is finally transported to the bin 3 by the conveyor belt.
本实用新型的有益效果为:The beneficial effects of the utility model are:
(1)污泥干燥过程中使用的热量均为循环水余热和太阳能等低成本热源,节省了大量干燥能源,带来了可观的经济效益,在实际工程应用中具有可操作性。(1) The heat used in the sludge drying process is low-cost heat sources such as circulating water waste heat and solar energy, which saves a lot of drying energy, brings considerable economic benefits, and is operable in practical engineering applications.
(2)该系统中循环水并不直接接触污泥,干燥空气也经过了除尘器脱除粉尘,并不因干燥污泥而产生二次污染。(2) The circulating water in the system does not directly contact the sludge, and the dry air also passes through the dust collector to remove dust, so there is no secondary pollution caused by drying the sludge.
(3)太阳能集热器的布置和使用,使得直接参与污泥干燥的空气温度可以达到更高程度,提升整个系统的热力参数,流化床式污泥加热器中传热温压得到提高,污泥的干燥程度也更大,即污泥脱水率也更高,提升了该系统的工作出力和运行效率。(3) The arrangement and use of solar collectors make the temperature of the air directly involved in sludge drying reach a higher level, improve the thermal parameters of the entire system, and improve the heat transfer temperature and pressure in the fluidized bed sludge heater. The drying degree of the sludge is also greater, that is, the sludge dehydration rate is also higher, which improves the work output and operating efficiency of the system.
(4)该系统整体的热力参数均为100℃以下,远远低于常规的污泥干燥设备主要干燥热源的温度,且不存在引燃的高温热源,因此在整个干燥过程中不会引起干燥设备内气体自燃或爆燃。故系统安全可靠性远高于同类型的污泥干燥设备。(4) The overall thermal parameters of the system are all below 100°C, which is far lower than the temperature of the main drying heat source of conventional sludge drying equipment, and there is no high-temperature heat source for ignition, so it will not cause drying during the entire drying process. Gas in the equipment spontaneously ignites or deflagrates. Therefore, the safety and reliability of the system is much higher than that of the same type of sludge drying equipment.
(5)该系统布置简单,流程短。系统热源主要来源于电厂的循环水和太阳能,而电厂循环水量大,即回收利用的热量也较大,具有很好的干燥潜力。所以该系统的单机处理能力大,可满足大规模的污泥干燥任务。(5) The system layout is simple and the process is short. The heat source of the system mainly comes from the circulating water and solar energy of the power plant, and the power plant has a large amount of circulating water, that is, the recovered heat is also relatively large, and has a good drying potential. Therefore, the system has a large stand-alone processing capacity and can meet large-scale sludge drying tasks.
(6)该系统使用循环水作为热源干燥污泥,循环水温度必将降低,因此对于使用空冷系统的火电机组,降低空冷系统能耗,最终降低凝汽器凝结水温,提高燃煤电厂热经济性;对于使用海水、河水作为冷却水的火电机组,最终排放的冷却水温度降低,将有效减少对江河海洋的热污染。(6) The system uses circulating water as a heat source to dry sludge, and the temperature of the circulating water will definitely decrease. Therefore, for thermal power units using an air-cooling system, the energy consumption of the air-cooling system will be reduced, and the condensing water temperature of the condenser will be reduced to improve the thermal economy of the coal-fired power plant. For thermal power units that use seawater and river water as cooling water, the temperature of the final discharged cooling water will be lowered, which will effectively reduce thermal pollution to rivers and oceans.
附图说明Description of drawings
下面结合附图和具体实施例对本实用新型作进一步的详细说明:Below in conjunction with accompanying drawing and specific embodiment the utility model is described in further detail:
图1是本实用新型系统适用于空冷机组的示意图。Fig. 1 is a schematic diagram of the utility model system applicable to an air-cooling unit.
图中标号表示如下:1、污泥加热器;2、流化床式干燥器;3、料仓;4、汽轮机;5、除尘器;6、太阳能集热板;7、凝汽器;8、鼓风机;9、空气-水换热器;10、冷却塔。The symbols in the figure are as follows: 1. Sludge heater; 2. Fluidized bed dryer; 3. Silo; 4. Steam turbine; 5. Dust collector; 6. Solar heat collector; 7. Condenser; 8 , Blower; 9, air-water heat exchanger; 10, cooling tower.
具体实施方式Detailed ways
本实用新型提供了一种利用电站余热耦合太阳能干燥城市污泥的系统,下面结合附图和具体实施方式对本实用新型的技术方案作进一步的说明。The utility model provides a system for drying urban sludge by utilizing waste heat of a power station coupled with solar energy. The technical solution of the utility model will be further described below in conjunction with the accompanying drawings and specific implementation methods.
如图1所示,污泥经粉碎后进入污泥加热器1,经循环水加热后落入流化床式干燥器2被温度更高的热空气干燥,最后由输煤皮带送往料仓3,留待下一步的资源利用。As shown in Figure 1, the sludge enters the sludge heater 1 after being pulverized, falls into the fluidized bed dryer 2 after being heated by circulating water, is dried by hot air at a higher temperature, and is finally sent to the silo by the coal conveyor belt 3. Leave it to the next resource utilization.
由汽轮机4排出来的乏汽在凝汽器7中凝结成水,放热给循环水,使循环水升温,凝结水从凝汽器7出来后完成电厂的汽水流程;循环水在凝汽器7中冷却汽轮机排汽,同时受热升温,在凝汽器出口7分为两路:一部分进入空气-水换热器9,加热来自鼓风机8的空气;另一部分经过旁路直接进入污泥加热器1作为污泥加热的主要热源。污泥加热器1出口和空气-水换热器9出口的循环水汇聚一块,返回电厂原来的循环水循环管道,被送到冷却塔10;空气被鼓风机8送入空气-水换热器9中被循环水加热,然后进入布置在换热器9出口的太阳能集热板6再次加热到更高的温度后输送到流化床式干燥器2中二次干燥污泥,带走污泥中的水分后,经过除尘器5除尘回收其携带粉尘,由电厂烟囱排放到大气中。The exhaust steam discharged from the steam turbine 4 is condensed into water in the condenser 7, and the heat is released to the circulating water to heat up the circulating water. After the condensed water comes out of the condenser 7, the steam-water process of the power plant is completed; the circulating water in the condenser In 7, the exhaust steam of the cooling steam turbine is heated at the same time, and it is divided into two paths at the condenser outlet 7: one part enters the air-water heat exchanger 9 to heat the air from the blower 8; the other part directly enters the sludge heater through a bypass 1 as the main heat source for sludge heating. The circulating water at the outlet of the sludge heater 1 and the outlet of the air-water heat exchanger 9 gathers together, returns to the original circulating water circulation pipe of the power plant, and is sent to the cooling tower 10; the air is sent into the air-water heat exchanger 9 by the blower 8 It is heated by circulating water, and then enters the solar collector plate 6 arranged at the outlet of the heat exchanger 9 to be heated again to a higher temperature and then transported to the fluidized bed dryer 2 to dry the sludge for the second time, taking away the sludge in the sludge After the moisture is removed, the dust carried by it is recovered by the dust collector 5, and is discharged into the atmosphere by the chimney of the power plant.
系统中循环水余热利用分别进行一次污泥加热一次空气加热,一次污泥加热为循环冷却水直接在污泥加热器1中对污泥进行加热升温,一次空气加热则在空气-水换热器9中循环水加热空气;系统中干燥介质-热空气在鼓风机送到空气-水换热器9中,与进入其中的循环水交换热量,空气被初次加热;在太阳能集热板6中,空气在太阳能作用下进行第二次加热。The waste heat of circulating water in the system is used for sludge heating and air heating respectively. The first sludge heating is circulating cooling water to directly heat up the sludge in the sludge heater 1, and the first air heating is in the air-water heat exchanger. The circulating water in 9 heats the air; the drying medium in the system - the hot air is sent to the air-water heat exchanger 9 by the blower, and exchanges heat with the circulating water entering it, and the air is heated for the first time; in the solar collector plate 6, the air The second heating is carried out under the action of solar energy.
本实用新型的系统同样适用于直流供水的火电机组,其不同点在于干燥系统后的循环冷却水直接排放到江河海洋之中,并不是冷却塔10,其余地方均一致,故在此并不详述。The system of the utility model is also applicable to thermal power units with direct current water supply. The difference is that the circulating cooling water after the drying system is directly discharged into the rivers and oceans instead of the cooling tower 10. The rest of the system is the same, so it is not detailed here. stated.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420265838.9U CN203960020U (en) | 2014-05-22 | 2014-05-22 | A kind of system of utilizing the dry municipal sludge of surplus heat of power plant coupled solar |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420265838.9U CN203960020U (en) | 2014-05-22 | 2014-05-22 | A kind of system of utilizing the dry municipal sludge of surplus heat of power plant coupled solar |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203960020U true CN203960020U (en) | 2014-11-26 |
Family
ID=51920629
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420265838.9U Expired - Fee Related CN203960020U (en) | 2014-05-22 | 2014-05-22 | A kind of system of utilizing the dry municipal sludge of surplus heat of power plant coupled solar |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203960020U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104045217A (en) * | 2014-05-22 | 2014-09-17 | 广东电网公司电力科学研究院 | Municipal sludge drying system utilizing power plant waste heat coupling solar energy |
| CN106049645A (en) * | 2016-07-05 | 2016-10-26 | 李俊峰 | On-line sludge cleaning system for cooling tower pool in thermal power plant |
| CN115959810A (en) * | 2022-12-05 | 2023-04-14 | 华北电力大学(保定) | Device for drying municipal sludge by indirect air cooling natural ventilation counter-flow cooling tower |
-
2014
- 2014-05-22 CN CN201420265838.9U patent/CN203960020U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104045217A (en) * | 2014-05-22 | 2014-09-17 | 广东电网公司电力科学研究院 | Municipal sludge drying system utilizing power plant waste heat coupling solar energy |
| CN106049645A (en) * | 2016-07-05 | 2016-10-26 | 李俊峰 | On-line sludge cleaning system for cooling tower pool in thermal power plant |
| CN115959810A (en) * | 2022-12-05 | 2023-04-14 | 华北电力大学(保定) | Device for drying municipal sludge by indirect air cooling natural ventilation counter-flow cooling tower |
| CN115959810B (en) * | 2022-12-05 | 2024-03-01 | 华北电力大学(保定) | An indirect air-cooled natural ventilation counterflow cooling tower drying urban sludge device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103708702B (en) | Energy-saving sludge drying device by utilizing recovery waste heat of vapor compression | |
| CN101251045B (en) | Biomass energy circulating power generation process and power generation system thereof | |
| CN102533383A (en) | Sodium-removing purification cyclic system of high-sodium coal | |
| CN112197278A (en) | System for coupling sludge drying incineration of secondary reheating power station boiler | |
| CN110715542A (en) | System for drying biomass and municipal domestic waste by using solar heat | |
| CN104534850B (en) | A kind of predrying system and method for raw coal low temperature utilizing flue gas, exhaust steam used heat | |
| CN102944024A (en) | Lignite thermal power generation system | |
| CN205619598U (en) | Dry complementary power generation system of supplementary air cooling unit of solar energy of integrated raw coal | |
| CN203960020U (en) | A kind of system of utilizing the dry municipal sludge of surplus heat of power plant coupled solar | |
| CN203203362U (en) | A system for drying lignite by using waste heat from power stations coupled with solar energy | |
| CN104045217A (en) | Municipal sludge drying system utilizing power plant waste heat coupling solar energy | |
| CN108658417B (en) | A coal-fired unit synergistic drying urban sludge system | |
| CN204529636U (en) | A kind of sludge drying and incineration system relying on heat power plant | |
| CN207313414U (en) | Utilize the sludge anhydration burning device of solar energy | |
| CN203653407U (en) | Energy-saving sludge drying device using solar energy and afterheat | |
| CN211040991U (en) | Coal-fired coupling sludge drying and incinerating system considering waste heat utilization | |
| CN107522382A (en) | A kind of sludge drying-incineration integrated system using solar source | |
| CN205170640U (en) | Utilize solar energy self -heating series connection heat pipe heat exchange efficient drying mud system | |
| CN104235818B (en) | The coal of fan mill powder process and the green electricity generation system of mud multifuel combustion | |
| CN202884958U (en) | Brown coal thermal power generation system | |
| CN207756595U (en) | A kind of electricity generation system of debirs clean utilization | |
| CN211546312U (en) | A low-temperature hydrothermal treatment system for sludge of coal-fired power station units | |
| CN216693565U (en) | Waste incineration device for co-combustion of sludge | |
| CN205974207U (en) | Energy recuperation type sludge drying system of burning | |
| CN115403239A (en) | Green low-carbon drying treatment process capable of utilizing energy resources for sludge |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20141126 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |