CN109928601A - Sludge deep drying method and system based on air heat pump - Google Patents
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- 239000010802 sludge Substances 0.000 title claims abstract description 107
- 238000001035 drying Methods 0.000 title claims abstract description 55
- 239000000843 powder Substances 0.000 claims abstract description 39
- 238000000034 method Methods 0.000 claims abstract description 17
- 238000001816 cooling Methods 0.000 claims abstract description 16
- 238000000926 separation method Methods 0.000 claims abstract description 14
- 238000003756 stirring Methods 0.000 claims abstract description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 10
- 238000010438 heat treatment Methods 0.000 claims abstract description 6
- 239000000463 material Substances 0.000 claims abstract description 3
- 238000009833 condensation Methods 0.000 claims description 19
- 230000005494 condensation Effects 0.000 claims description 19
- 230000008859 change Effects 0.000 claims description 3
- 239000007787 solid Substances 0.000 claims description 3
- 238000004064 recycling Methods 0.000 claims description 2
- 238000010410 dusting Methods 0.000 claims 11
- 238000007791 dehumidification Methods 0.000 claims 6
- 238000013019 agitation Methods 0.000 claims 1
- 239000003570 air Substances 0.000 abstract description 96
- 238000010298 pulverizing process Methods 0.000 abstract description 23
- 239000002245 particle Substances 0.000 abstract description 5
- 239000012080 ambient air Substances 0.000 abstract description 3
- 239000011343 solid material Substances 0.000 abstract description 3
- 230000008569 process Effects 0.000 description 6
- 239000010865 sewage Substances 0.000 description 4
- 230000018044 dehydration Effects 0.000 description 3
- 238000006297 dehydration reaction Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
本发明公开了基于空气热泵的污泥深度干化方法及系统。将待处理剩余污泥加入污泥粉化干化装置中,使含水率30%~55%的待处理污泥被粉化破碎成为粒径为30~250μm的污泥粉粒,然后通入干燥空气在搅拌条件下与污泥粉粒混合,使污泥粉粒进行干化得到污泥干粉,同时干燥空气变成夹带着污泥干粉的低温含湿空气。将夹带着污泥干粉的低温含湿空气通过分离装置进行气粉分离,分离下来的固体物质即为污泥干粉料。污泥干粉料含水率为15%~25%。分离后的低温含湿空气进入冷凝除湿器冷凝除水后,成为低低温空气;将低低温空气送入空气热泵加热重新成为干燥空气,进行重复利用。而冷却空气吸收的热量再回到空气热泵热交换给低低温空气。本发明具有污泥深度干化且直接利用环境空气作为热源,节能高效等优点。
The invention discloses a method and system for deep drying of sludge based on an air heat pump. Add the remaining sludge to be treated into the sludge pulverization and drying device, so that the sludge to be treated with a moisture content of 30% to 55% is pulverized and broken into sludge powder with a particle size of 30 to 250 μm, and then passed into the drying process. The air is mixed with the sludge powder under stirring conditions, and the sludge powder is dried to obtain the sludge dry powder. The low-temperature moisture-containing air carrying the sludge dry powder is separated from the gas powder through the separation device, and the separated solid material is the sludge dry powder material. The moisture content of the sludge dry powder is 15% to 25%. The separated low-temperature moisture-containing air enters the condensing dehumidifier to condense and remove water, and becomes low-low temperature air; the low-low temperature air is sent to the air heat pump for heating and becomes dry air again for reuse. The heat absorbed by the cooling air is returned to the air heat pump for heat exchange to the low and low temperature air. The invention has the advantages of deep drying of sludge, direct use of ambient air as a heat source, energy saving and high efficiency, and the like.
Description
技术领域technical field
本发明涉及基于空气热泵的污泥深度干化方法及系统,尤其涉及一种剩余污泥深度脱水的方法及工艺系统,属于环保技术领域的污水处理厂剩余污泥处理子领域。The invention relates to a method and system for deep drying of sludge based on an air heat pump, in particular to a method and a process system for deep dewatering of excess sludge, which belongs to the sub-field of waste sludge treatment of sewage treatment plants in the technical field of environmental protection.
背景技术Background technique
随着我国社会和城市化的发展,城市污水的产生量在不断增长,相应的污水处理设施的数量也随之增加,污水处理后的副产物——剩余污泥的产生量也越来越大。截止2017年,我国剩余污泥年产量已超过4000万吨,而无害化处理率不足10%。如何妥善处理处置这些源源不断产生、数量日益庞大的污泥已成为我国环境保护方面亟待解决的问题。With the development of my country's society and urbanization, the amount of urban sewage is increasing, and the number of corresponding sewage treatment facilities is also increasing. . As of 2017, the annual output of excess sludge in my country has exceeded 40 million tons, and the harmless treatment rate is less than 10%. How to properly handle and dispose of these continuously generated and increasingly large sludge has become an urgent problem to be solved in my country's environmental protection.
国内大部分污水处理厂产生的剩余污泥,其含水率一般在80%以上。污泥脱水是其处理过程中的关键步骤。而污泥难以深度脱水的特点,已成为限制污泥无害化、资源化处理的瓶颈问题。The excess sludge produced by most domestic sewage treatment plants generally has a moisture content of more than 80%. Sludge dewatering is a key step in its treatment process. The difficulty of deep dewatering of sludge has become a bottleneck problem that restricts the harmless and resourceful treatment of sludge.
目前,污泥脱水干化的主要工艺有太阳能干燥、热干化、调理-压滤脱水等。其中太阳能干燥工艺利用太阳能的热效应,可将污泥含水率降至10%以下,达到深度干化的目的,但是由于其占地面积达、处理周期长、受天气变化影响大,较难广泛应用。热干化技术是通过直接加热或间接加热的方式将污泥中水分蒸发去除,污泥含水率可降至40%以下,而进一步降低含水率则所需将能耗大幅上升;调理-压滤脱水技术是剩余污泥经过调理剂改性处理,提高污泥脱水性能,再经过压滤机压榨脱水,污泥含水率可降至60%。以上工艺能够快速脱除污泥中的水分,但是脱水程度有限,较难实现污泥的深度干化(含水率≤20%)。At present, the main processes of sludge dewatering and drying include solar drying, thermal drying, conditioning-filter press dehydration, etc. Among them, the solar drying process utilizes the thermal effect of solar energy, which can reduce the moisture content of the sludge to below 10% and achieve the purpose of deep drying. . Thermal drying technology evaporates the water in the sludge through direct heating or indirect heating, and the water content of the sludge can be reduced to less than 40%, and further reduction of the water content requires a significant increase in energy consumption; conditioning - filter press The dewatering technology is that the excess sludge is modified by a conditioner to improve the dewatering performance of the sludge, and then pressed and dewatered by a filter press, and the moisture content of the sludge can be reduced to 60%. The above process can quickly remove the moisture in the sludge, but the degree of dehydration is limited, and it is difficult to achieve deep drying of the sludge (water content ≤ 20%).
因此,进一步降低热干化或机械脱水工艺产生的半干污泥的含水率,快速高效的实现剩余污泥的深度干化,是目前的发展方向。Therefore, it is the current development direction to further reduce the moisture content of the semi-dry sludge produced by thermal drying or mechanical dehydration process and realize the deep drying of excess sludge quickly and efficiently.
发明内容SUMMARY OF THE INVENTION
本发明旨在提供一种基于空气热泵的污泥深度干化方法及系统,利用空气热泵从环境空气中获取热量既形成干燥空气又制得冷却空气,在干化污泥的同时使系统整体更加节能高效。The present invention aims to provide a method and system for deep drying of sludge based on an air heat pump, which utilizes the air heat pump to obtain heat from ambient air to form both dry air and cooling air, and makes the overall system more efficient while drying the sludge. Energy efficient.
本发明通过以下技术方案实现:The present invention is achieved through the following technical solutions:
基于空气热泵的污泥深度干化方法,所述方法包括:Sludge deep drying method based on air heat pump, the method includes:
将待处理剩余污泥加入污泥粉化干化装置中,使待处理污泥被粉化破碎成为粒径为30~250μm的污泥粉粒,然后通入干燥空气在搅拌条件下与污泥粉粒混合,使污泥粉粒进行干化得到污泥干粉,同时干燥空气变成夹带着污泥干粉的低温含湿空气;The remaining sludge to be treated is added to the sludge pulverization and drying device, so that the sludge to be treated is pulverized and broken into sludge powder with a particle size of 30-250 μm, and then drying air is introduced to mix with the sludge under stirring conditions. The powder is mixed to make the sludge powder dry to obtain the sludge dry powder, and the drying air becomes the low-temperature moist air carrying the sludge dry powder at the same time;
将夹带着污泥干粉的低温含湿空气通过分离装置进行气固分离,分离下来的固体物质即为污泥干粉料;分离后的低温含湿空气进入冷凝除湿器冷凝除水后,成为低低温空气;将所述低低温空气送入空气热泵加热成为干燥空气,并将干燥空气送入污泥粉化干化装置在搅拌条件下与污泥粉粒混合,使污泥粉粒进行干化。The low-temperature moisture-containing air carrying the sludge dry powder is separated from the gas and solid through the separation device, and the separated solid material is the sludge dry powder material; the separated low-temperature moisture-containing air enters the condensing dehumidifier to condense and remove water, and becomes a low-low temperature Air; the low-low temperature air is sent to the air heat pump to be heated to become dry air, and the dry air is sent to the sludge pulverization and drying device to be mixed with the sludge powder under stirring conditions to dry the sludge powder.
所述方法还包括:The method also includes:
将新鲜空气送入空气热泵与低低温空气换热,使新鲜空气降温成为冷却空气的同时使低低温空气升温成为干燥空气;将干燥空气送入污泥粉化干化装置对污泥粉粒进行干燥,实现干燥空气的循环使用。The fresh air is sent into the air heat pump to exchange heat with the low and low temperature air, so that the fresh air is cooled to become cooling air, and the low and low temperature air is heated to become dry air; Dry, realize the recycling of dry air.
所述方法还包括:The method also includes:
将冷却空气送入所述冷凝除湿器与所述低温含湿空气间壁式换热,使低温含湿空气冷凝除水后成为低低温空气,同时冷却空气升温后成为温热空气;将温热空气送入空气热泵作为热源供低低温空气换热升温,同时温热空气降温重新成为冷却空气回到所述冷凝除湿器重复使用。The cooling air is sent into the condensation dehumidifier and the low-temperature moisture-containing air is subjected to wall heat exchange, so that the low-temperature moisture-containing air is condensed and dewatered to become low-low temperature air, and the cooling air is heated to become warm air; The incoming air heat pump is used as a heat source for heat exchange of low and low temperature air to heat up, and at the same time, the temperature of warm air is cooled down and returned to the condensing dehumidifier for repeated use.
上述技术方案中,所述剩余污泥的含水率为35%~50%;所述污泥干粉的含水率为15%~25%。In the above technical solution, the moisture content of the excess sludge is 35% to 50%; the moisture content of the dry sludge powder is 15% to 25%.
基于空气热泵的污泥深度干化系统,包括污泥粉化干化装置、分离装置、冷凝除湿器和空气热泵;所述污泥粉化干化装置包括连通的粉化室和干化室,所述粉化室设有进料装置;所述分离装置分别与所述污泥粉化干化装置和冷凝除湿器相连;所空气述热泵分别与所述冷凝除湿器和所述污泥粉化干化装置相连。A sludge deep drying system based on an air heat pump includes a sludge pulverization and drying device, a separation device, a condensation dehumidifier and an air heat pump; the sludge pulverization and drying device includes a connected pulverization chamber and a drying chamber, The pulverization chamber is provided with a feeding device; the separation device is respectively connected with the sludge pulverization and drying device and the condensation dehumidifier; the air and the heat pump are respectively connected with the condensation dehumidifier and the sludge pulverizer The drying device is connected.
上述技术方案中,所述污泥粉化干化装置的粉化室和干化室内均设置有螺旋搅拌装置;所述干化室设有进气口与所述空气热泵相连。In the above technical solution, both the pulverizing chamber and the drying chamber of the sludge pulverizing and drying device are provided with a screw stirring device; the drying chamber is provided with an air inlet which is connected to the air heat pump.
本发明具有以下优点及有益效果:干化效果提高,将污泥干化的经济含水率由40%大幅降至20%以下;通过空气源热泵,以环境中的空气作为热源,相比于热干化技术,更加节能高效。The invention has the following advantages and beneficial effects: the drying effect is improved, and the economical moisture content of sludge drying is greatly reduced from 40% to below 20%; Drying technology, more energy-saving and efficient.
附图说明Description of drawings
图1为本发明所涉及的基于空气热泵的污泥深度干化系统示意图。FIG. 1 is a schematic diagram of a sludge deep drying system based on an air heat pump according to the present invention.
图中:1–污泥粉化干化装置;2–分离装置;3–冷凝除湿器;4–空气热泵。In the figure: 1 – sludge pulverization and drying device; 2 – separation device; 3 – condensation dehumidifier; 4 – air heat pump.
具体实施方式Detailed ways
下面结合附图对本发明的具体实施方式及工作过程作进一步的说明。The specific embodiments and working process of the present invention will be further described below with reference to the accompanying drawings.
本申请文件中的上、下、左、右、前和后等方位用语是基于附图所示的位置关系而建立的。附图不同,则相应的位置关系也有可能随之发生变化,故不能以此理解为对保护范围的限定。Orientation terms such as upper, lower, left, right, front and rear in this application document are established based on the positional relationship shown in the accompanying drawings. If the drawings are different, the corresponding positional relationship may also change accordingly, so this should not be construed as a limitation on the protection scope.
如图1所示,基于空气热泵的污泥深度干化系统,包括污泥粉化干化装置1、分离装置2、冷凝除湿器3和空气热泵4。污泥粉化干化装置1包括连通的粉化室和干化室,粉化室设有进料装置。污泥粉化干化装置1的粉化室和干化室内均设置有螺旋搅拌装置。干化室设有进气口通入干燥空气。分离装置2分别与污泥粉化干化装置1和冷凝除湿器3相连。空气热泵4分别与冷凝除湿器3和污泥粉化干化装置1相连。进气口与空气热泵4相连。As shown in FIG. 1 , the air heat pump-based sludge deep drying system includes a sludge pulverization and drying device 1 , a separation device 2 , a condensation dehumidifier 3 and an air heat pump 4 . The sludge pulverizing and drying device 1 includes a connected pulverizing chamber and a drying chamber, and the pulverizing chamber is provided with a feeding device. Both the pulverizing chamber and the drying chamber of the sludge pulverizing and drying device 1 are provided with a screw stirring device. The drying chamber is provided with an air inlet to introduce dry air. The separation device 2 is respectively connected with the sludge pulverization and drying device 1 and the condensation dehumidifier 3 . The air heat pump 4 is respectively connected with the condensation dehumidifier 3 and the sludge pulverizing and drying device 1 . The air inlet is connected to the air heat pump 4 .
将含水率为35%~50%的待处理剩余污泥通过进料装置加入污泥粉化干化装置1中,使待处理污泥首先在粉化室内被螺旋搅拌装置粉化破碎成为粒径为30~250μm的污泥粉粒。然后通过进气口通入干燥空气,在螺旋搅拌装置1500-3000r/min的搅拌强度下搅拌8-20min,使干燥空气与污泥粉粒混合均匀并发生充分的气水交换反应,使污泥粉粒进行干化得到污泥干粉,含水率降为15%~25%。同时干燥空气变成夹带着污泥干粉的低温含湿空气。其中一个实施例为干燥空气为环境空气加热后的低温干燥空气,其湿度为20%~40%、温度25℃~50℃,与剩余污泥气水交换反应后,变成湿度60%~90%的低温含湿空气。The excess sludge to be treated with a moisture content of 35% to 50% is added to the sludge pulverization and drying device 1 through the feeding device, so that the sludge to be treated is firstly pulverized and broken into particle sizes by the screw stirring device in the pulverizing chamber. It is 30~250μm sludge powder. Then, dry air is introduced through the air inlet, and stirred for 8-20 minutes at the stirring intensity of 1500-3000r/min of the screw stirring device, so that the dry air and the sludge particles are mixed evenly and a sufficient gas-water exchange reaction occurs, so that the sludge The powder particles are dried to obtain dry sludge powder, and the moisture content is reduced to 15% to 25%. At the same time, the drying air becomes the low-temperature moist air entrained with the dry sludge powder. One of the embodiments is that the dry air is low-temperature dry air heated by ambient air, its humidity is 20% to 40%, and its temperature is 25°C to 50°C. % of low temperature moist air.
将夹带着污泥干粉的低温含湿空气通过分离装置2进行气粉分离,分离下来的固体物质即为污泥干粉料。分离装置2可以选用除尘器。分离后的低温含湿空气进入冷凝,同时将冷却空气送入冷凝除湿器3与低温含湿空气间壁式换热,使低温含湿空气冷凝除水后成为低低温空气,冷凝水排出冷凝除湿器。将低低温空气送入空气热泵4加热成为干燥空气,并将干燥空气送入污泥粉化干化装置1在搅拌条件下与污泥粉粒混合,使污泥粉粒进行干化。即空气在空气热泵4、污泥粉化干化装置1和分离装置2以及冷凝除湿器3之间形成循环使用。通常循环10次后作为废气,进行净化处理后排放,此时从空气热泵4补入新鲜空气。The low-temperature moisture-containing air carrying the dry sludge powder is passed through the separation device 2 for gas-powder separation, and the separated solid material is the dry sludge powder. Separation device 2 can choose dust collector. The separated low-temperature moisture-containing air enters the condensation, and at the same time, the cooling air is sent to the condensation dehumidifier 3 to exchange heat with the low-temperature moisture-containing air, so that the low-temperature moisture-containing air is condensed and dewatered to become low-temperature air, and the condensed water is discharged from the condensation dehumidifier. . The low and low temperature air is sent to the air heat pump 4 to be heated into dry air, and the dry air is sent to the sludge pulverization and drying device 1 to be mixed with the sludge powder under stirring conditions to dry the sludge powder. That is, the air is circulated among the air heat pump 4 , the sludge pulverization and drying device 1 , the separation device 2 and the condensation dehumidifier 3 . Usually after 10 cycles, it is used as exhaust gas, and it is discharged after purification treatment. At this time, fresh air is supplied from the air heat pump 4 .
新鲜空气一方面作为干燥空气的补充源,另一方面作为冷却空气的补充源。首先利用新鲜空气在空气热泵4中作为热源与低低温空气换热,在使低低温空气升温成为干燥空气的同时,新鲜空气降温成为冷却空气,并进入冷凝除湿器3作为冷却介质。冷却空气在冷凝除湿器3中从低温含湿空气中吸收热量从而温度升高成为温热空气,再将温热空气送入空气热泵4作为热源。在上述实施例中,冷却空气为5℃~15℃,换热后温度升到8~18℃。The fresh air serves as a supplementary source for drying air on the one hand and cooling air on the other hand. First, the fresh air is used as a heat source in the air heat pump 4 to exchange heat with the low and low temperature air. When the low and low temperature air is heated to become dry air, the fresh air is cooled to become cooling air, and enters the condensing dehumidifier 3 as a cooling medium. The cooling air absorbs heat from the low-temperature humid air in the condensing dehumidifier 3 so that the temperature rises to become warm air, and then the warm air is sent to the air heat pump 4 as a heat source. In the above embodiment, the cooling air is 5°C to 15°C, and the temperature rises to 8 to 18°C after heat exchange.
以上所述仅为本发明的优选实施例而已,并不用于限制本发明,对于本领域的技术人员来说,本发明可以有各种更改和变化。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。The above descriptions are only preferred embodiments of the present invention, and are not intended to limit the present invention. For those skilled in the art, the present invention may have various modifications and changes. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention shall be included within the protection scope of the present invention.
Claims (6)
Priority Applications (1)
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