CN102815852A - Complete processing unit for sludge drying - Google Patents
Complete processing unit for sludge drying Download PDFInfo
- Publication number
- CN102815852A CN102815852A CN2012102918428A CN201210291842A CN102815852A CN 102815852 A CN102815852 A CN 102815852A CN 2012102918428 A CN2012102918428 A CN 2012102918428A CN 201210291842 A CN201210291842 A CN 201210291842A CN 102815852 A CN102815852 A CN 102815852A
- Authority
- CN
- China
- Prior art keywords
- sludge
- scraper
- tail gas
- cylindrical shell
- treatment device
- 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
- 239000010802 sludge Substances 0.000 title claims abstract description 138
- 238000001035 drying Methods 0.000 title claims abstract description 29
- 238000001816 cooling Methods 0.000 claims abstract description 27
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 16
- 238000004891 communication Methods 0.000 claims description 6
- 238000009833 condensation Methods 0.000 claims description 4
- 230000005494 condensation Effects 0.000 claims description 4
- 230000008676 import Effects 0.000 claims 3
- 230000000694 effects Effects 0.000 abstract description 5
- 230000007613 environmental effect Effects 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000007789 gas Substances 0.000 description 44
- 238000000034 method Methods 0.000 description 5
- 239000010865 sewage Substances 0.000 description 5
- 238000010586 diagram Methods 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 208000005156 Dehydration Diseases 0.000 description 2
- 239000004566 building material Substances 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000006297 dehydration reaction Methods 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004043 dyeing Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 239000010985 leather Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Landscapes
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Abstract
本发明涉及一种污泥干化成套处理装置,属于环境保护领域。本发明包括刮板式污泥干燥机、分散式进料装置、尾气冷却塔、污泥焚烧设备;刮板式污泥干燥机上端与尾气冷却塔连接,下端与污泥焚烧设备连接,分散式进料装置安装在刮板式污泥干燥机上。本发明结构简单、干化效果好、干化均匀、产品质量好、成本低、环保,能实现污泥一体化处理,生产效率高。
The invention relates to a complete treatment device for sludge drying, which belongs to the field of environmental protection. The invention comprises a scraper type sludge dryer, a distributed feeding device, a tail gas cooling tower, and sludge incineration equipment; the upper end of the scraper type sludge dryer is connected with the tail gas cooling tower, and the lower end is connected with the sludge incineration equipment, and the distributed feeding The device is installed on the scraper sludge dryer. The invention has the advantages of simple structure, good drying effect, uniform drying, good product quality, low cost, environmental protection, integrated treatment of sludge and high production efficiency.
Description
技术领域 technical field
本发明涉及一种污泥干化处理装置,特别涉及一种污泥干化成套处理装置,属于环境保护领域。 The invention relates to a sludge drying treatment device, in particular to a sludge drying complete treatment device, which belongs to the field of environmental protection.
背景技术 Background technique
污泥主要出现在污水处理厂中,是污水处理后的主要副产物,且污泥的数量非常巨大,不易处理,这令水处理行业人士非常头疼,仅我国每年生活污水处理产生的污泥量就达到了上亿吨,再加上日前我国经济水平发展迅速,大量工业投入生产,随之而来的就是会产生大量的工业污泥,例如造纸污泥、印染污泥、制革污泥、油泥污泥等等。污泥具有含水量高,富含成分复杂等特点,污泥中一般含有流失有价原料和潜在热,同时富集高浓度的重金属等污染物,如果采用直接焚烧的传统方法对高含水量的污泥进行处理,需要对污泥进行浓缩、消化、调节、脱水,然后再焚烧或填埋,这样处理污泥会造成污泥中含有的有价原料等可利用资源的流失,对环境造成严重的污染,目前普遍采用的是机械干燥的方法处理污泥,将污泥通过干燥机进行干化,然后再对干化的污泥进行再回收利用、焚烧,但机械脱水处理效果不是太理想,造成在运输过程中的一些麻烦,例如体积依旧很大,含水量依旧很高,等等。 Sludge mainly appears in sewage treatment plants and is the main by-product after sewage treatment. The amount of sludge is very large and difficult to handle. This makes people in the water treatment industry very troubled. Only the amount of sludge produced by domestic sewage treatment in my country It has reached hundreds of millions of tons. In addition, my country's economic level has developed rapidly recently, and a large number of industries have been put into production, followed by a large amount of industrial sludge, such as papermaking sludge, printing and dyeing sludge, leather sludge, Oil sludge and so on. Sludge has the characteristics of high water content and complex components. Sludge generally contains lost valuable raw materials and latent heat, and at the same time enriches high concentrations of heavy metals and other pollutants. If the traditional method of direct incineration is used to treat high water content For sludge treatment, it is necessary to concentrate, digest, adjust, dehydrate the sludge, and then incinerate or landfill it. Such treatment of sludge will cause the loss of valuable raw materials and other available resources contained in the sludge, which will seriously affect the environment. At present, the method of mechanical drying is generally used to treat sludge, and the sludge is dried through a dryer, and then the dried sludge is recycled and incinerated, but the effect of mechanical dehydration treatment is not very ideal. It caused some troubles in the transportation process, such as the volume is still very large, the water content is still high, and so on.
干化之后的污泥经过进一步处理,具有广泛的用途,例如可以经过厌氧消化等处理后在农业领域中用作复合肥,又可以经过堆肥处理后在林业领域用做景观绿化,还可以合成燃料来焚烧发电,可做成建材或铺路等在建材领域得到应用,因此将污泥经干燥机干化后,既能使污泥中的原料等有价成分和潜在热得到回收利用,又能减少焚烧污泥的耗用和环境污染,也就是说污泥干化是实现污泥成为可利用资源的重要步骤,而实现污泥干化的设备目前主要有四种,即转窑式污泥干燥机、流化床式污泥干燥机、桨叶式污泥干燥机、圆盘式干燥机等。以上类型设备大部分都会存在着糊料严重,干燥物料的质量欠佳,效率低等缺点,在市场上销售的圆盘式干燥机也存在着能耗大、效率低等缺点。 After further treatment, the dried sludge has a wide range of uses. For example, it can be used as compound fertilizer in the agricultural field after anaerobic digestion, and can be used as landscape greening in the forestry field after composting. It can also be synthesized It can be used in the field of building materials as building materials or road paving. Therefore, after the sludge is dried by a dryer, valuable components such as raw materials and potential heat in the sludge can be recycled and reused. To reduce the consumption of incineration sludge and environmental pollution, that is to say, sludge drying is an important step to make sludge a usable resource, and there are currently four main types of equipment for sludge drying, namely rotary kiln sludge Dryer, fluidized bed sludge dryer, paddle sludge dryer, disc dryer, etc. Most of the above types of equipment have shortcomings such as heavy paste, poor quality of dried materials, and low efficiency. The disc dryers sold in the market also have shortcomings such as high energy consumption and low efficiency.
发明内容 Contents of the invention
本发明的目的是提供一种结构简单、干化处理效果好、高效、环保、节能,能实现污泥一体化处理的污泥干化成套处理装置。 The object of the present invention is to provide a complete set of sludge drying treatment device with simple structure, good drying treatment effect, high efficiency, environmental protection, energy saving, and capable of realizing integrated treatment of sludge.
本发明按以下技术方案实现:一种污泥干化成套处理装置,包括刮板式污泥干燥机1、分散式进料装置2、尾气冷却塔12、污泥焚烧设备23;刮板式污泥干燥机1上端与尾气冷却塔12连接,下端与污泥焚烧设备23连接,分散式进料装置2安装在刮板式污泥干燥机1上。
The present invention is realized according to the following technical solutions: a complete set of sludge drying treatment device, including a scraper
所述刮板式污泥干燥机1包括安全阀8、电动机9、圆形平板19、筒体20、正刮板21、反刮板22;刮板式污泥干燥机1的筒体20内安装有转轴10,电动机9安装在转轴10的上方,安全阀8安置在刮板式污泥干燥机1的筒体20上端,正刮板21、反刮板22安置在转轴10上,刮板式污泥干燥机1的筒体20两侧设有蒸汽连通管7,蒸汽连通管7与污泥焚烧设备23连接,筒体20顶端设有尾气出口11,下端靠近污泥焚烧设备23处设有通气口5,圆形平板19与蒸汽连通管7连接,刮板式污泥干燥机1的筒体20下侧设有出料口6。
The scraper
所述分散式进料装置2上设有进料总管3、分散进料口4,分散进料口4穿过筒体20通入圆形平板19上。
The
所述尾气冷却塔12塔壁为两层,内层为尾气通道,外层为污泥通道,在污泥未到达进料口4之前先经过尾气冷却塔12。所述尾气冷却塔12外层上侧设有污泥进口13,另一侧下方设有剩余污泥出口14,内层上侧设有冷凝尾气出口16,下侧设有尾气进口15、冷凝出水口17,冷凝出水口17处设有出水开关18。所述筒体20上部顶盖采用圆形尖顶形状,圆形平板19呈空心原状,四周高、中间低。所述筒体20的尾气出口11与尾气冷却塔12的尾气进口15连接。所述剩余污泥出口14与分散式进料装置2上的进料总管3连接。
The tower wall of the tail
所述圆形平板19与正刮板21、反刮板22之间有一定空隙,正刮板21和反刮板22起的作用不同,正刮板21主要将污泥平摊在圆形平板19上,反刮板22则是将干化后的污泥刮起并脱落到中心,并进入污泥焚烧设备23。所述的污泥焚烧设备23主要是将干化后的污泥进行焚烧,为整个污泥干化成套装置提供热量,通过通气口5向污泥焚烧设备23提供充足的氧气。
There is a certain gap between the circular
工作原理为:剩余污泥由进料总管3进入各分散进料口4,分散进料口4通入圆形平板19一侧,随着电动机9的转动,带动中间转轴10及转轴10上的正刮板21、反刮板22一起转动,正刮板21主要将从分散进料口4进来的剩余污泥摊平,通过圆形平板19的高温,将已经摊平的剩余污泥进行干化脱水,脱水之后由与正刮板21对称的反刮板22将已经干化理想的剩余污泥进行刮除,刮除过程是由四周向中间进行,最终各圆形平板19的干化污泥全部从中间落下,落入位于下部的污泥焚烧设备23,通过通气口5的换气,将干化污泥进行不断焚烧,产生大量的蒸汽,蒸汽由蒸汽连通管7与圆形平板19相通,通过蒸汽将热量为整个污泥干化装置提供热量,如果蒸汽系统内气压过大,则会由上部的安全阀8进行自动排泄,确保蒸汽系统内压力的稳定,这样反反复复的进行,使整个系统不断的运行。在污泥干化过程中由于剩余污泥中含有大量水分,因此整个系统水分含量很高,并会产生大量的含有高湿度的尾气,尾气通过尾气出口11排除进入尾气冷却塔12,尾气冷却塔12是通过进入进料总管3之前的剩余污泥进行冷却,这样除了起到冷却的作用之外,还可以提高进料的初始温度,便于系统效率的提高,尾气经过冷凝之后,冷凝水通过冷凝出水口17排出并回流至污水处理厂前端,由污水处理厂进行处理,冷凝后的尾气通过冷凝尾气出口16进入尾气处理装置进行处理。
The working principle is: the remaining sludge enters the
本发明具有以下有益效果: The present invention has the following beneficial effects:
1、结构简单、干化效果好、干化均匀、产品质量好、成本低; 1. Simple structure, good drying effect, uniform drying, good product quality and low cost;
2、连续干化、实现了污泥一体化处理、生产效率高; 2. Continuous drying realizes integrated treatment of sludge and high production efficiency;
3、采用干化后的污泥进行焚烧产热,避免污泥中含有大量的有机物等物质,外加能耗低,在做到了节能的同时也有很好的环保效果。 3. The dried sludge is used for incineration to generate heat to avoid a large amount of organic matter and other substances in the sludge, and the energy consumption is low, which not only saves energy, but also has a good environmental protection effect.
附图说明 Description of drawings
图1为本发明的外观示意图; Fig. 1 is the appearance schematic diagram of the present invention;
图2为本发明的主视结构示意图; Fig. 2 is the front view structure schematic diagram of the present invention;
图3为本发明的侧视结构示意图; Fig. 3 is a side view structural representation of the present invention;
图4为本发明刮板与圆形平板示意图。 Fig. 4 is a schematic diagram of a scraper and a circular flat plate of the present invention.
图中各标号为:1:刮板式污泥干燥机、2:分散式进料装置、3:进料总管、4:分散进料口、5:通气口、6:出料口、7:蒸汽连通管、8:安全阀、9:电动机、10:转轴、11:尾气出口、12:尾气冷却塔、13:污泥进口、14:剩余污泥出口、15:尾气进口、16:冷凝尾气出口、17:冷凝出水口、18:出水开关、19:圆形平板、20:筒体、21:正刮板、22:反刮板、23:干化污泥焚烧设备。 The labels in the figure are: 1: Scraper type sludge dryer, 2: Dispersed feeding device, 3: Feed main pipe, 4: Dispersed feed inlet, 5: Ventilation port, 6: Discharge port, 7: Steam Connecting pipe, 8: Safety valve, 9: Motor, 10: Rotating shaft, 11: Exhaust gas outlet, 12: Exhaust gas cooling tower, 13: Sludge inlet, 14: Excess sludge outlet, 15: Exhaust gas inlet, 16: Condensed exhaust gas outlet , 17: condensate outlet, 18: water outlet switch, 19: circular plate, 20: cylinder, 21: positive scraper, 22: reverse scraper, 23: dried sludge incineration equipment.
具体实施方式 Detailed ways
下面结合附图和实施例,对本发明作进一步说明,但本发明的内容并不限于所述范围。 The present invention will be further described below in conjunction with the accompanying drawings and embodiments, but the content of the present invention is not limited to the stated scope.
实施例1:如图1-4所示,一种污泥干化成套处理装置,包括刮板式污泥干燥机1、分散式进料装置2、尾气冷却塔12、污泥焚烧设备23;刮板式污泥干燥机1上端与尾气冷却塔12连接,下端与污泥焚烧设备23连接,分散式进料装置2安装在刮板式污泥干燥机1上。
Example 1: As shown in Figures 1-4, a complete set of sludge drying treatment device includes a
刮板式污泥干燥机1包括安全阀8、电动机9、圆形平板19、筒体20、正刮板21、反刮板22;刮板式污泥干燥机1的筒体20内安装有转轴10,电动机9安装在转轴10的上方,安全阀8安置在刮板式污泥干燥机1的筒体20左侧上端,正刮板21、反刮板22安置在转轴10上,刮板式污泥干燥机1的筒体20两侧设有蒸汽连通管7,蒸汽连通管7与污泥焚烧设备23连接,筒体20顶端右侧设有尾气出口11,下端靠近污泥焚烧设备23处设有通气口5,圆形平板19与蒸汽连通管7连接,刮板式污泥干燥机1的筒体20右下侧设有出料口6。
The scraper
分散式进料装置2上设有进料总管3、分散进料口4,分散进料口4穿过筒体20通入圆形平板19上。
The distributed
尾气冷却塔12塔壁为两层,内层为尾气通道,外层为污泥通道。尾气冷却塔12外层左上侧设有污泥进口13,另一侧下方设有剩余污泥出口14,内层右上侧设有冷凝尾气出口16,下侧设有尾气进口15、冷凝出水口17,冷凝出水口17处设有出水开关18。筒体20上部顶盖采用圆形尖顶形状,圆形平板19呈空心原状,四周高、中间低。筒体20的尾气出口11与尾气冷却塔12的尾气进口15连接。剩余污泥出口14与分散式进料装置2上的进料总管3连接。
The tower wall of the tail
实施例2:如图1-4所示,一种污泥干化成套处理装置,包括刮板式污泥干燥机1、分散式进料装置2、尾气冷却塔12、污泥焚烧设备23;刮板式污泥干燥机1上端与尾气冷却塔12连接,下端与污泥焚烧设备23连接,分散式进料装置2安装在刮板式污泥干燥机1上。
Example 2: As shown in Figures 1-4, a complete set of sludge drying treatment device, including a
刮板式污泥干燥机1包括安全阀8、电动机9、圆形平板19、筒体20、正刮板21、反刮板22;刮板式污泥干燥机1的筒体20内安装有转轴10,电动机9安装在转轴10的上方,安全阀8安置在刮板式污泥干燥机1的筒体20右侧上端,正刮板21、反刮板22安置在转轴10上,刮板式污泥干燥机1的筒体20两侧设有蒸汽连通管7,蒸汽连通管7与污泥焚烧设备23连接,顶端左侧设有尾气出口11,下端靠近污泥焚烧设备23处设有通气口5,圆形平板19与蒸汽连通管7连接,刮板式污泥干燥机1的筒体20左下侧设有出料口6。
The scraper
分散式进料装置2上设有进料总管3、分散进料口4,分散进料口4穿过筒体20通入圆形平板19上。
The distributed
尾气冷却塔12塔壁为两层,内层为尾气通道,外层为污泥通道。尾气冷却塔12外层右上侧设有污泥进口13,另一侧下方设有剩余污泥出口14,内层左上侧设有冷凝尾气出口16,下侧设有尾气进口15、冷凝出水口17,冷凝出水口17处设有出水开关18。筒体20上部顶盖采用圆形尖顶形状,圆形平板19呈空心原状,四周高、中间低。筒体20的尾气出口11与尾气冷却塔12的尾气进口15连接。剩余污泥出口14与分散式进料装置2上的进料总管3连接。
The tower wall of the tail
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012102918428A CN102815852A (en) | 2012-08-16 | 2012-08-16 | Complete processing unit for sludge drying |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012102918428A CN102815852A (en) | 2012-08-16 | 2012-08-16 | Complete processing unit for sludge drying |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN102815852A true CN102815852A (en) | 2012-12-12 |
Family
ID=47300359
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012102918428A Pending CN102815852A (en) | 2012-08-16 | 2012-08-16 | Complete processing unit for sludge drying |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102815852A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103482847A (en) * | 2013-09-18 | 2014-01-01 | 华南理工大学 | Sludge conditioner and sludge conditioning method thereof |
| CN108558101A (en) * | 2018-01-29 | 2018-09-21 | 内蒙古苏德环保科技有限公司 | Wastewater treatment method |
| CN109534650A (en) * | 2018-12-28 | 2019-03-29 | 南京工业大学 | Solid-liquid separation device and use method thereof |
| CN111434631A (en) * | 2019-01-11 | 2020-07-21 | 湖南鼎诚合力环保科技发展有限公司 | Surplus sludge drying processing treatment device |
| CN113898952A (en) * | 2021-10-30 | 2022-01-07 | 北京华能长江环保科技研究院有限公司 | Multi-stage sludge drying and incineration device |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1312863A (en) * | 1998-09-02 | 2001-09-12 | 保尔·沃特公司 | Process for heat-treating residues containing heavy metals and iron oxides |
| CN1823016A (en) * | 2003-05-14 | 2006-08-23 | 生物3D应用公司 | Waste heat recovery system and method and its application in treating waste with high water content |
| CN201000259Y (en) * | 2007-01-26 | 2008-01-02 | 张志霄 | Shaft-type stirred sludge multi-stage secondary steam reuse drying device |
| CN202350055U (en) * | 2011-12-16 | 2012-07-25 | 奚亚明 | Multi-layer multi-segment sludge drying and incinerating integrated furnace |
| CN202361381U (en) * | 2011-10-28 | 2012-08-01 | 青海大地环境工程技术有限公司 | Dry-residue residual-oil burning device for oily sludge |
| CN202849226U (en) * | 2012-08-16 | 2013-04-03 | 昆明理工大学 | Complete treating device for sludge drying |
-
2012
- 2012-08-16 CN CN2012102918428A patent/CN102815852A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1312863A (en) * | 1998-09-02 | 2001-09-12 | 保尔·沃特公司 | Process for heat-treating residues containing heavy metals and iron oxides |
| CN1823016A (en) * | 2003-05-14 | 2006-08-23 | 生物3D应用公司 | Waste heat recovery system and method and its application in treating waste with high water content |
| CN201000259Y (en) * | 2007-01-26 | 2008-01-02 | 张志霄 | Shaft-type stirred sludge multi-stage secondary steam reuse drying device |
| CN202361381U (en) * | 2011-10-28 | 2012-08-01 | 青海大地环境工程技术有限公司 | Dry-residue residual-oil burning device for oily sludge |
| CN202350055U (en) * | 2011-12-16 | 2012-07-25 | 奚亚明 | Multi-layer multi-segment sludge drying and incinerating integrated furnace |
| CN202849226U (en) * | 2012-08-16 | 2013-04-03 | 昆明理工大学 | Complete treating device for sludge drying |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103482847A (en) * | 2013-09-18 | 2014-01-01 | 华南理工大学 | Sludge conditioner and sludge conditioning method thereof |
| CN103482847B (en) * | 2013-09-18 | 2016-05-04 | 华南理工大学 | Mud quality-adjusting device and mud hardening and tempering method thereof |
| CN108558101A (en) * | 2018-01-29 | 2018-09-21 | 内蒙古苏德环保科技有限公司 | Wastewater treatment method |
| CN109534650A (en) * | 2018-12-28 | 2019-03-29 | 南京工业大学 | Solid-liquid separation device and use method thereof |
| CN111434631A (en) * | 2019-01-11 | 2020-07-21 | 湖南鼎诚合力环保科技发展有限公司 | Surplus sludge drying processing treatment device |
| CN111434631B (en) * | 2019-01-11 | 2022-06-07 | 湖南鼎诚合力环保科技发展有限公司 | Surplus sludge drying processing treatment device |
| CN113898952A (en) * | 2021-10-30 | 2022-01-07 | 北京华能长江环保科技研究院有限公司 | Multi-stage sludge drying and incineration device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101774743B (en) | Latent heat recoverable multi-phase change sludge drying method and device | |
| CN101857350B (en) | Cement kiln waste gas indirect drying treatment and sludge utilization device and process method | |
| CN105254147B (en) | A kind of sludge superheated vapor dries the triple utilization device and methods of exhaust steam residual heat | |
| CN108298791A (en) | A kind of novel multi-functional sludge heat pump desiccation machine | |
| CN107337335A (en) | A kind of sludge drying and the equipment and technique of charing | |
| CN102815852A (en) | Complete processing unit for sludge drying | |
| CN107686224A (en) | A kind of vacuum dehydration drying equipment and technique | |
| CN202849226U (en) | Complete treating device for sludge drying | |
| CN104150732B (en) | A kind of mud two-stage anhydration system | |
| CN203582671U (en) | Sludge dewatering machine | |
| CN101746940A (en) | Dewatering sludge alkaline type semi-desiccation processing method of sewage treatment plants | |
| CN205300185U (en) | Thermal balance formula drying -machine | |
| CN105693052A (en) | Dyeing sludge deep dehydrating-drying treatment device and process | |
| CN206666356U (en) | One kind is used for chemical engineering sludge dewatered drying device | |
| CN206255975U (en) | Sewage sludge continuous band and the complete processing system of heat pump desiccation | |
| CN108249733A (en) | A kind of low energy consumption municipal sludge heat treatment dehydration device and method | |
| CN202272828U (en) | Device for making domestic sludge into fertilizers | |
| CN202576181U (en) | Sludge dryer special for hollow blade | |
| CN205133368U (en) | Triple devices that utilize of mud superheated steam drying exhaust steam waste heat | |
| CN203653407U (en) | Energy-saving sludge drying device using solar energy and afterheat | |
| CN203095826U (en) | Sludge drying machine utilizing waste heat | |
| CN206157011U (en) | City domestic sewage excess sludge mummification device | |
| CN206721013U (en) | A kind of microwave type paper mill sludge dries separation integrated apparatus | |
| CN202988945U (en) | Movable sludge drying device | |
| CN110066095A (en) | A kind of municipal sludge low temperature drying and other treatment system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20121212 |