CN108007107A - A kind of solar energy desiccation factory concurrent heating system and application method - Google Patents
A kind of solar energy desiccation factory concurrent heating system and application method Download PDFInfo
- Publication number
- CN108007107A CN108007107A CN201711290858.6A CN201711290858A CN108007107A CN 108007107 A CN108007107 A CN 108007107A CN 201711290858 A CN201711290858 A CN 201711290858A CN 108007107 A CN108007107 A CN 108007107A
- Authority
- CN
- China
- Prior art keywords
- steam
- air
- heat exchanger
- heating system
- desiccation
- 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.)
- Pending
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/06—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/12—Treatment of sludge; Devices therefor by de-watering, drying or thickening
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22D—PREHEATING, OR ACCUMULATING PREHEATED, FEED-WATER FOR STEAM GENERATION; FEED-WATER SUPPLY FOR STEAM GENERATION; CONTROLLING WATER LEVEL FOR STEAM GENERATION; AUXILIARY DEVICES FOR PROMOTING WATER CIRCULATION WITHIN STEAM BOILERS
- F22D11/00—Feed-water supply not provided for in other main groups
- F22D11/02—Arrangements of feed-water pumps
- F22D11/06—Arrangements of feed-water pumps for returning condensate to boiler
-
- F26B21/40—
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Mechanical Engineering (AREA)
- Chemical & Material Sciences (AREA)
- Water Supply & Treatment (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Hydrology & Water Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Organic Chemistry (AREA)
- Combustion & Propulsion (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Abstract
本发明公开了一种太阳能干化厂辅热系统及使用方法。它包括干化大棚内安装的通风机以及干化大棚内铺设的地暖系统,干化大棚的一侧设置有蒸汽空气换热器,蒸汽空气换热器的空气输入端连接有鼓风机,蒸汽空气换热器的蒸汽输入端经过蒸汽阀门连接锅炉系统,蒸汽空气换热器的出风端经过风管连接通风机,蒸汽空气换热器的出水端经过水管连接地暖系统,通风机、鼓风机以及蒸汽阀门均通过统一控制系统控制。采用上述系统和方法后,大大提升了沼渣干化效果,蒸汽换热完后的冷凝高温热水进入地暖系统后继续加热干化床上的沼渣,与沼渣换热完成后,冷凝低温冷水回收循环使用,具有蒸汽余热回收、水循环利用等优点,彻底实现了真正的节能减排。
The invention discloses an auxiliary heating system of a solar drying plant and a using method thereof. It includes a ventilator installed in the drying greenhouse and a floor heating system laid in the drying greenhouse. A steam-air heat exchanger is installed on one side of the drying greenhouse. The air input end of the steam-air heat exchanger is connected to a blower. The steam input end of the heater is connected to the boiler system through the steam valve, the air outlet end of the steam-air heat exchanger is connected to the fan through the air pipe, the water outlet end of the steam-air heat exchanger is connected to the floor heating system through the water pipe, the fan, the blower and the steam valve All are controlled by a unified control system. After adopting the above system and method, the drying effect of the biogas residue is greatly improved. After the steam heat exchange, the condensed high-temperature hot water enters the floor heating system and continues to heat the biogas residue on the drying bed. After the heat exchange with the biogas residue is completed, the low-temperature cold water is condensed Recycling and recycling, with the advantages of steam waste heat recovery, water recycling, etc., completely realized the real energy saving and emission reduction.
Description
技术领域technical field
本发明涉及一种太阳能干化厂的辅热系统,具体地说是一种太阳能干化厂辅热系统,属于节能环保技术领域。The invention relates to an auxiliary heating system of a solar drying plant, in particular to an auxiliary heating system of a solar drying plant, belonging to the technical field of energy saving and environmental protection.
背景技术Background technique
在餐厨废弃物与污泥协同处理过程中,太阳能干化厂是将产气后餐厨垃圾与污泥的混合物沼渣资源化利用的重要区域,太阳能干化是指借助传统温室干燥技术,结合当代自动化技术的发展,利用太阳能这种清洁能源作为沼渣干化的主要能量来源,采用太阳能干化处理沼渣过程无臭、无三废,可实现零排放清洁型生产,含水60-80%左右的沼渣经太阳能干化后,沼渣含水可降至30%左右,干化后可作为营养土使用,实现节能、减排、资源化利用的目的。In the process of co-processing of kitchen waste and sludge, the solar drying plant is an important area for resource utilization of the mixture of kitchen waste and sludge after gas production. Solar drying refers to the use of traditional greenhouse drying technology. Combined with the development of modern automation technology, solar energy, a clean energy, is used as the main energy source for biogas residue drying, and the process of using solar energy to dry biogas residues is odorless and free of three wastes, and can achieve zero-emission clean production, with a water content of 60-80% After the left and right biogas residues are dried by solar energy, the water content of the biogas residues can be reduced to about 30%. After drying, they can be used as nutrient soil to achieve the goals of energy saving, emission reduction, and resource utilization.
太阳能干化厂一般有太阳能干化大棚、布料机、污泥翻抛机、通风机等设备设施。脱水沼渣经过输送机送入干化大棚,由布料机均匀布置在干化床上,翻抛机和通风机不断地对沼渣进行混合、破碎、通风来实现干化。在夏天,阳光充足时,暖房温度可达50℃以上,沼渣出料含水率可降至30%,干化效果明显,但是在冬季,由于光照时间短,气温低等因素影响,沼渣出料含水率只在55%左右,为解决这一问题,很多厂家通过增加空调、热泵等设备提高干化大棚内部空气温度,事实证明,虽然干化效果得到了提高,但是电能消耗太大,失去了节能减排的意义。Solar drying plants generally have equipment and facilities such as solar drying greenhouses, distributing machines, sludge turning machines, and ventilators. The dehydrated biogas residue is sent to the drying greenhouse through the conveyor, and is evenly arranged on the drying bed by the distribution machine. The turning machine and the fan continuously mix, crush and ventilate the biogas residue to realize drying. In summer, when there is sufficient sunshine, the temperature of the greenhouse can reach above 50°C, and the moisture content of the biogas residue can be reduced to 30%, and the drying effect is obvious. The moisture content of the material is only about 55%. In order to solve this problem, many manufacturers increase the air temperature inside the drying greenhouse by adding air conditioners, heat pumps and other equipment. Facts have proved that although the drying effect has been improved, the power consumption is too large. The significance of energy saving and emission reduction.
发明内容Contents of the invention
本发明要解决的技术问题是提供一种能耗低、干化效果好,彻底实现节能减排目的的太阳能干化厂辅热系统及使用方法。The technical problem to be solved by the present invention is to provide an auxiliary heating system for a solar drying plant with low energy consumption, good drying effect, and a thorough realization of energy saving and emission reduction and its use method.
为了解决上述技术问题,本发明的太阳能干化厂辅热系统,包括干化大棚内安装的通风机以及干化大棚内铺设的地暖系统,干化大棚的一侧设置有蒸汽空气换热器,蒸汽空气换热器的空气输入端连接有能够使外部空气进入到蒸汽空气换热器内的鼓风机,蒸汽空气换热器的蒸汽输入端经过蒸汽阀门连接锅炉系统,蒸汽空气换热器的出风端经过风管连接通风机,蒸汽空气换热器的出水端经过水管连接地暖系统,通风机、鼓风机以及蒸汽阀门均通过统一控制系统控制,通风机、鼓风机以及蒸汽阀门通过控制系统控制并能够使空气和蒸汽进入到蒸汽空气换热器内加热换热,经过蒸汽空气换热器加热换热后的蒸汽经过通风机进入到干化大棚内与沼渣进行强制对流,经过蒸汽空气换热器加热换热产生的蒸汽水经过地暖系统循环加热干化大棚内的沼渣并流至锅炉系统内循环使用。In order to solve the above technical problems, the auxiliary heating system of the solar drying plant of the present invention includes a ventilator installed in the drying booth and a floor heating system laid in the drying booth, and a steam-air heat exchanger is arranged on one side of the drying booth. The air input end of the steam-air heat exchanger is connected with a blower that can make external air enter the steam-air heat exchanger, the steam input end of the steam-air heat exchanger is connected to the boiler system through a steam valve, and the air outlet of the steam-air heat exchanger The outlet end of the steam-air heat exchanger is connected to the floor heating system through the water pipe. The ventilator, blower and steam valve are all controlled by a unified control system. The ventilator, blower and steam valve are controlled by the control system and can be used Air and steam enter the steam-air heat exchanger to heat and exchange heat. After being heated by the steam-air heat exchanger, the steam enters the drying greenhouse through the fan for forced convection with the biogas residue, and is heated by the steam-air heat exchanger. The steam water generated by the heat exchange is circulated through the floor heating system to heat and dry the biogas residue in the greenhouse and flows to the boiler system for recycling.
所述干化大棚设置有干化床,所述蒸汽空气换热器安装在干化大棚的干化床的末端。The drying booth is provided with a drying bed, and the steam-air heat exchanger is installed at the end of the drying bed in the drying booth.
所述蒸汽空气换热器为管壳式换热器或热管式换热器。The steam-air heat exchanger is a shell-and-tube heat exchanger or a heat pipe heat exchanger.
所述地暖系统埋在干化大棚的干化床下,所述地暖系统呈U形排列布满整个干化床。The floor heating system is buried under the drying bed of the drying greenhouse, and the floor heating system is arranged in a U shape and covers the entire drying bed.
一种采用上述太阳能干化厂辅热系统的使用方法,包括以下步骤:A method for using the auxiliary heating system of the above-mentioned solar drying plant, comprising the following steps:
A:打开鼓风机,将冷空气经过空气输入端进入到蒸汽空气换热器内;A: Turn on the blower and let the cold air enter the steam-air heat exchanger through the air input port;
B:蒸汽阀门打开,蒸汽通入至蒸汽空气换热器内,与冷空气换热,使冷空气温度升高,高温蒸汽冷却成高温热水流入地暖系统内,高温热水进入地暖系统,将热量传递给干化床表面上沼渣,与此同时,被加热后的高温空气,通过干化大棚内的通风机与沼渣进行强制对流;B: The steam valve is opened, the steam is passed into the steam-air heat exchanger, and exchanges heat with the cold air, so that the temperature of the cold air rises, the high-temperature steam is cooled into high-temperature hot water and flows into the floor heating system, and the high-temperature hot water enters the floor heating system. The heat is transferred to the biogas residue on the surface of the drying bed, and at the same time, the heated high-temperature air is forced to convect with the biogas residue through the fan in the drying greenhouse;
C:通过关闭控制系统,停止换热加热整个过程。C: By turning off the control system, stop the whole process of heat exchange and heating.
所述步骤B中,高温热水经过地暖系统后形成降低温度冷凝成低温冷水并回到锅炉系统内继续循环利用。In the step B, the high-temperature hot water passes through the floor heating system to reduce the temperature and condense into low-temperature cold water, which is then returned to the boiler system for further recycling.
采用上述系统和方法后,在传统太阳能干化厂的基础上,利用厂区剩余蒸汽通过蒸汽空气换热器加热空气,再通过鼓风机将高温空气送入干化厂参与生产,大大提升了沼渣干化效果,蒸汽换热完后的冷凝高温热水进入地暖系统后继续加热干化床上的沼渣,与沼渣换热完成后,冷凝低温冷水回收循环使用,该技术方案和传统空调、热泵等辅热设备相比,避免了现有辅热系统电能消耗过大的缺点,同时还具有蒸汽余热回收、水循环利用等优点,彻底实现了真正的节能减排。After adopting the above system and method, on the basis of the traditional solar drying plant, the remaining steam in the plant area is used to heat the air through the steam-air heat exchanger, and then the high-temperature air is sent to the drying plant to participate in production through the blower, which greatly improves the dryness of the biogas residue. The condensed high-temperature hot water after the steam heat exchange enters the floor heating system and continues to heat the biogas residue on the drying bed. After the heat exchange with the biogas residue is completed, the condensed low-temperature cold water is recycled and recycled. This technical solution is different from traditional air conditioners, heat pumps, etc. Compared with auxiliary heating equipment, it avoids the disadvantage of excessive power consumption of the existing auxiliary heating system, and also has the advantages of steam waste heat recovery, water recycling, etc., and thoroughly realizes real energy saving and emission reduction.
附图说明Description of drawings
图1为本发明太阳能干化厂辅热系统的结构示意图。Fig. 1 is a structural schematic diagram of the auxiliary heating system of the solar drying plant of the present invention.
具体实施方式Detailed ways
下面结合附图和具体实施方式,对本发明的太阳能干化厂辅热系统及使用方法作进一步详细说明。The auxiliary heating system and usage method of the solar drying plant of the present invention will be further described in detail in conjunction with the accompanying drawings and specific implementation methods.
本发明针对太阳能干化厂因冬季气温低,光照不足而导致干化效果不理想的问题,重新构思,利用剩余蒸汽通过蒸汽空气换热器加热空气,结合地暖提高干化厂内部温度,从而提高沼渣干化效率,其采用的技术方案如下:The present invention aims at the problem of unsatisfactory drying effect caused by low winter temperature and insufficient light in solar drying plants. It reconceives that the remaining steam is used to heat the air through a steam-air heat exchanger, and combined with floor heating to increase the internal temperature of the drying plant, thereby improving Biogas residue drying efficiency, the technical scheme adopted is as follows:
如图所示,本发明的太阳能干化厂辅热系统,包括干化大棚内安装的通风机1以及干化大棚内铺设的地暖水管2,干化大棚设置有干化床,干化大棚的一侧设置有蒸汽空气换热器3,蒸汽空气换热器是进行热量交换主要设备,蒸汽空气换热器3安装在干化大棚的干化床的末端,不影响翻抛机的正常运行,蒸汽空气换热器3的空气输入端连接有能够使外部空气进入到蒸汽空气换热器3内的鼓风机4,蒸汽空气换热器3的蒸汽输入端经过蒸汽阀门5连接锅炉系统,蒸汽空气换热器3的出风端经过风管连接通风机1,蒸汽空气换热器3的出水端经过水管连接地暖水管2,地暖水管2埋在干化大棚的干化床下,地暖水管2呈U形排列布满整个干化床,同时考虑到传热效果不宜埋深,通风机1、鼓风机4以及蒸汽阀门5均通过统一控制系统控制,通风机1、鼓风机4以及蒸汽阀门5通过控制系统控制并能够使空气和蒸汽进入到蒸汽空气换热器3内加热换热,经过蒸汽空气换热器3加热换热后的蒸汽经过通风机1进入到干化大棚内与沼渣进行强制对流,经过蒸汽空气换热器3加热换热产生的蒸汽水经过地暖水管2循环加热干化大棚内的沼渣并流至锅炉系统内循环使用。As shown in the figure, the auxiliary heating system of the solar energy drying plant of the present invention includes a ventilator 1 installed in the drying booth and a floor heating water pipe 2 laid in the drying booth. One side is provided with a steam-air heat exchanger 3, the steam-air heat exchanger is the main equipment for heat exchange, the steam-air heat exchanger 3 is installed at the end of the drying bed of the drying greenhouse, which does not affect the normal operation of the turning machine. The air input end of the steam-air heat exchanger 3 is connected with a blower 4 capable of allowing external air to enter the steam-air heat exchanger 3, and the steam input end of the steam-air heat exchanger 3 is connected to the boiler system through a steam valve 5, and the steam-air heat exchanger The air outlet end of the heater 3 is connected to the fan 1 through the air pipe, and the water outlet end of the steam-air heat exchanger 3 is connected to the floor heating water pipe 2 through the water pipe. The floor heating water pipe 2 is buried under the drying bed of the drying greenhouse, and the floor heating water pipe 2 is U-shaped. Arranged all over the entire drying bed, and considering the heat transfer effect should not be buried deep, the ventilator 1, blower 4 and steam valve 5 are all controlled by a unified control system, and the ventilator 1, blower 4 and steam valve 5 are controlled by the control system and The air and steam can enter the steam-air heat exchanger 3 for heating and heat exchange, and the steam heated and exchanged by the steam-air heat exchanger 3 enters the drying greenhouse through the ventilator 1 for forced convection with the biogas residue, and passes through the steam The steam water generated by the heat exchange of the air heat exchanger 3 is circulated through the floor heating water pipe 2 to heat and dry the biogas slag in the greenhouse and flow to the boiler system for recycling.
其中,所说的蒸汽空气换热器3优选为管壳式换热器或热管式换热器,但不限于此,所说的鼓风机的主要功能是将太阳能干化大棚外的冷空气抽入蒸汽空气换热器,并将换热完的热空气吹入到干化大棚内部,随后热空气通过干化厂原有的通风机1干化沼渣。Wherein, said steam-to-air heat exchanger 3 is preferably a shell-and-tube heat exchanger or a heat pipe heat exchanger, but is not limited thereto. The main function of said blower is to draw cold air outside the solar drying greenhouse into The steam-air heat exchanger blows the hot air after heat exchange into the drying greenhouse, and then the hot air passes through the original fan 1 of the drying plant to dry the biogas residue.
通过上述结构设计,高温高压蒸汽进入蒸汽空气换热器和冷空气换热后变为高温水流出,从蒸汽空气换热器中流出的热水进入地暖水管,持续加热干化床表面沼渣,由于地暖使用的是清洁蒸汽冷凝水,故与沼渣换热完后冷水可回收继续循环利用,整个仅鼓风机消耗少量电能,与传统空调、热泵辅热系统相比节约了大量电能,成本更为低廉,同时蒸汽水还可循环使用,实现了真正的节能减排,另外,本发明可对外适配多种类型太阳能干化厂。Through the above structural design, high-temperature and high-pressure steam enters the steam-air heat exchanger and exchanges heat with cold air to become high-temperature water, and the hot water flowing out of the steam-air heat exchanger enters the floor heating water pipe to continuously heat the biogas residue on the surface of the drying bed. Since the floor heating uses clean steam condensate, the cold water can be recycled and recycled after the heat exchange with biogas residues. Only the blower consumes a small amount of electric energy. Compared with traditional air conditioning and heat pump auxiliary heating systems, it saves a lot of electric energy and costs more. It is cheap, and steam water can be recycled at the same time, which realizes real energy saving and emission reduction. In addition, the invention can be externally adapted to various types of solar drying plants.
一种采用上述太阳能干化厂辅热系统的使用方法,包括以下步骤:A method for using the auxiliary heating system of the above-mentioned solar drying plant, comprising the following steps:
A:打开鼓风机,将冷空气经过空气输入端进入到蒸汽空气换热器内;A: Turn on the blower and let the cold air enter the steam-air heat exchanger through the air input port;
B:蒸汽阀门打开,蒸汽通入至蒸汽空气换热器内,与冷空气换热,使冷空气温度升高,高温蒸汽冷却成高温热水流入地暖水管2内,高温热水进入地暖水管,将热量传递给干化床表面上沼渣,提高温度,与此同时,被加热后的高温空气,通过干化大棚内的通风机与沼渣进行强制对流,提升干化厂内部气温,加快沼渣干化速度,最终降低沼渣含水率;B: The steam valve is opened, the steam is passed into the steam-air heat exchanger, and exchanges heat with the cold air, so that the temperature of the cold air rises, the high-temperature steam is cooled into high-temperature hot water and flows into the floor heating water pipe 2, and the high-temperature hot water enters the floor heating water pipe, The heat is transferred to the biogas residue on the surface of the drying bed to increase the temperature. At the same time, the heated high-temperature air is forced to convect with the biogas residue through the fan in the drying greenhouse to increase the internal temperature of the drying plant and accelerate the drying of the biogas residue. Drying speed, finally reduce the moisture content of biogas residue;
C:通过关闭控制系统,停止换热加热整个过程,所说的控制系统为自动控制系统,其主要用来控制设备远程或手动开启,做到连接各个设备,维持干化厂内恒定温度的自动化控制,由此通过该控制系统即可现场手动操作也可远程操作,也可根据厂内通风机开启情况做到全自动启停。C: Stop the whole process of heat exchange and heating by closing the control system. The control system is an automatic control system, which is mainly used to control the remote or manual opening of the equipment, so as to connect various equipment and maintain a constant temperature in the drying plant. Control, so through the control system, it can be operated manually on site or remotely, and can also be automatically started and stopped according to the opening of the fan in the factory.
进一步地,步骤B中,高温热水经过地暖系统后降低温度冷凝成低温冷水并回到锅炉系统内继续循环利用。Further, in step B, the high-temperature hot water passes through the floor heating system and then lowers its temperature to condense into low-temperature cold water and returns to the boiler system for further recycling.
以江苏某城市有机质处理中心为例,将餐厨废弃物与生活污泥协同处理,混合物在厌氧罐厌氧发酵产生沼气,提纯后并网使用,沼渣经过脱水机房深度脱水,含水率降至60%左右送入太阳能干化厂进一步干化。Taking an organic matter treatment center in a city in Jiangsu as an example, the kitchen waste and domestic sludge are co-processed. The mixture is anaerobically fermented in an anaerobic tank to produce biogas, which is purified and connected to the grid for use. About 60% is sent to the solar drying plant for further drying.
冬天气温较低,光照不足时,如图1所示:当干化厂内部通风机1开启时,辅热系统鼓风机4联动开启,蒸汽阀门5打开,150℃饱和干蒸气进入蒸汽空气换热器3内,将空气加热至50-60℃,由鼓风机通过风管送入干化厂参与沼渣干化生产,在换热器中的蒸汽冷却为80℃左右的高温热水进入地暖系统循环加热干化床表面沼渣,换热完后的蒸汽水约25℃,流出地暖系统至厂内锅炉房循环使用,当干化厂内部通风机1关闭后,系统自动关闭1使用该辅热系统后,干化厂内部温度能达到45℃以上,沼渣含水率可降至30%。When the temperature is low in winter and the light is insufficient, as shown in Figure 1: when the internal ventilator 1 of the drying plant is turned on, the blower 4 of the auxiliary heating system is turned on in conjunction, the steam valve 5 is turned on, and the saturated dry steam at 150°C enters the steam-air heat exchanger 3, the air is heated to 50-60°C, and sent by the blower to the drying plant through the air duct to participate in the drying of biogas residues, and the steam in the heat exchanger is cooled to high-temperature hot water at about 80°C, which enters the floor heating system for circulation heating The biogas slag on the surface of the drying bed, the steam water after the heat exchange is about 25°C, flows out of the floor heating system to the boiler room in the plant for recycling, when the internal ventilation fan 1 of the drying plant is turned off, the system will automatically shut down 1 After using the auxiliary heating system , The internal temperature of the drying plant can reach above 45°C, and the moisture content of the biogas residue can be reduced to 30%.
Claims (6)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711290858.6A CN108007107A (en) | 2017-12-08 | 2017-12-08 | A kind of solar energy desiccation factory concurrent heating system and application method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201711290858.6A CN108007107A (en) | 2017-12-08 | 2017-12-08 | A kind of solar energy desiccation factory concurrent heating system and application method |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN108007107A true CN108007107A (en) | 2018-05-08 |
Family
ID=62057196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201711290858.6A Pending CN108007107A (en) | 2017-12-08 | 2017-12-08 | A kind of solar energy desiccation factory concurrent heating system and application method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN108007107A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947202A (en) * | 2018-08-06 | 2018-12-07 | 宁夏中科国通新能源有限公司 | A kind of sludge compound thermal anhydration system and its method |
| CN110566921A (en) * | 2019-08-19 | 2019-12-13 | 江苏京泓生态环保有限公司 | Gas boiler waste heat recycling device and method |
| CN110642491A (en) * | 2019-10-12 | 2020-01-03 | 江苏泓润生物质能科技有限公司 | Waste heat recovery method for hot water coil of anaerobic tank system |
| CN110665945A (en) * | 2019-10-12 | 2020-01-10 | 江苏泓润生物质能科技有限公司 | Waste heat recovery and recycling method used in organic waste treatment process |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050246919A1 (en) * | 2002-08-28 | 2005-11-10 | Degremont | Installation for drying waste, in particular wastewater purifying sludge |
| FR2927693A1 (en) * | 2008-02-15 | 2009-08-21 | Egis Eau Sa | Installation for drying sludge obtained from sewage treatment and liquid effluents, comprises greenhouse with a heat floor, solar heating device in greenhouse, device for geothermally heating coolant fluid, and device for returning sludge |
| CN101948230A (en) * | 2010-09-13 | 2011-01-19 | 苏州奥泰斯环保科技发展有限公司 | Sludge drying treatment system |
| CN104478191A (en) * | 2014-12-01 | 2015-04-01 | 北京高能时代环境技术股份有限公司 | Solar sludge drying treatment device and solar sludge drying treatment process |
| CN106630533A (en) * | 2016-11-21 | 2017-05-10 | 盐城工学院 | A solar energy sludge drying device |
| CN107421266A (en) * | 2017-09-18 | 2017-12-01 | 无锡市泰顺植绒机械厂 | Solar drying machine |
| CN207649257U (en) * | 2017-12-08 | 2018-07-24 | 江苏泓润生物质能科技有限公司 | A kind of auxiliary thermal of solar energy desiccation factory |
-
2017
- 2017-12-08 CN CN201711290858.6A patent/CN108007107A/en active Pending
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20050246919A1 (en) * | 2002-08-28 | 2005-11-10 | Degremont | Installation for drying waste, in particular wastewater purifying sludge |
| FR2927693A1 (en) * | 2008-02-15 | 2009-08-21 | Egis Eau Sa | Installation for drying sludge obtained from sewage treatment and liquid effluents, comprises greenhouse with a heat floor, solar heating device in greenhouse, device for geothermally heating coolant fluid, and device for returning sludge |
| CN101948230A (en) * | 2010-09-13 | 2011-01-19 | 苏州奥泰斯环保科技发展有限公司 | Sludge drying treatment system |
| CN104478191A (en) * | 2014-12-01 | 2015-04-01 | 北京高能时代环境技术股份有限公司 | Solar sludge drying treatment device and solar sludge drying treatment process |
| CN106630533A (en) * | 2016-11-21 | 2017-05-10 | 盐城工学院 | A solar energy sludge drying device |
| CN107421266A (en) * | 2017-09-18 | 2017-12-01 | 无锡市泰顺植绒机械厂 | Solar drying machine |
| CN207649257U (en) * | 2017-12-08 | 2018-07-24 | 江苏泓润生物质能科技有限公司 | A kind of auxiliary thermal of solar energy desiccation factory |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108947202A (en) * | 2018-08-06 | 2018-12-07 | 宁夏中科国通新能源有限公司 | A kind of sludge compound thermal anhydration system and its method |
| CN110566921A (en) * | 2019-08-19 | 2019-12-13 | 江苏京泓生态环保有限公司 | Gas boiler waste heat recycling device and method |
| CN110642491A (en) * | 2019-10-12 | 2020-01-03 | 江苏泓润生物质能科技有限公司 | Waste heat recovery method for hot water coil of anaerobic tank system |
| CN110665945A (en) * | 2019-10-12 | 2020-01-10 | 江苏泓润生物质能科技有限公司 | Waste heat recovery and recycling method used in organic waste treatment process |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203323206U (en) | Smoke discharge waste heat recovery circular energy saving system | |
| CN202809328U (en) | Heat pump clothes dryer | |
| CN203848526U (en) | Novel solar drying system | |
| CN110440530B (en) | An industrial waste heat composite solar greenhouse drying system and method | |
| CN207006735U (en) | A kind of waste gas residual heat reclaims high/low temperature energy-saving dryer | |
| CN105021015A (en) | Superhigh-temperature heat pump drying system | |
| CN108007107A (en) | A kind of solar energy desiccation factory concurrent heating system and application method | |
| CN104061698B (en) | Salar light-gathering formula thermal-arrest baking oven | |
| CN109293407A (en) | A kind of kitchen waste quick fertilizer making device and method | |
| CN101629777A (en) | In-store drying process device of solar-assisted heat pump | |
| CN207435292U (en) | A kind of coupled electricity-generation system using smoke residual heat to dry sludge | |
| CN104930610A (en) | Multifunctional, efficient and energy-saving total-heat recovery unit | |
| CN202476421U (en) | Double heat source drying device applied to tobacco flue-curing | |
| CN204902523U (en) | Super high temperature heat pump drying system | |
| CN208170887U (en) | A kind of drying unit of double heat sources | |
| CN211823510U (en) | Intelligent energy-saving heat-preservation drying room | |
| CN207649257U (en) | A kind of auxiliary thermal of solar energy desiccation factory | |
| CN210907370U (en) | Organic refuse treatment waste heat recovery device | |
| WO2022032495A1 (en) | Heating device for garbage pool of garbage incineration power plant | |
| CN102139166A (en) | Method for drying carbide slag slurry | |
| CN205717965U (en) | A kind of Winter-summer dual purpose energy-saving evaporation cooling system of combination roofing water-retention | |
| CN207692651U (en) | A kind of energy saving and environment friendly pig house | |
| CN108534482A (en) | One grows tobacco radiative oven dry dehumidification system | |
| CN115088625A (en) | Building method of solar dehumidifying and cooling pig house | |
| CN206338852U (en) | Plant's hot air recycling system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20180508 |
|
| RJ01 | Rejection of invention patent application after publication |