CN203128381U - Integrated sludge deep dehydrating drying machine - Google Patents
Integrated sludge deep dehydrating drying machine Download PDFInfo
- Publication number
- CN203128381U CN203128381U CN 201320100970 CN201320100970U CN203128381U CN 203128381 U CN203128381 U CN 203128381U CN 201320100970 CN201320100970 CN 201320100970 CN 201320100970 U CN201320100970 U CN 201320100970U CN 203128381 U CN203128381 U CN 203128381U
- Authority
- CN
- China
- Prior art keywords
- sludge
- mud
- gear type
- drying machine
- heat
- 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
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model relates to the field of environmental protection equipment and in particular relates to an integrated sludge deep dehydrating drying machine. The integrated sludge deep dehydrating drying machine comprises a controllable flocculation device (1), a full-automatic electronic control system, an overlaid spiral sludge dehydrating machine (8), a gear type sludge drying machine (25) and an air purifying system (23). The integrated sludge deep dehydrating drying machine is characterized in that the controllable flocculation device (1) is internally provided with a liquid level meter (2), an overflow pipeline (3), a sewage inlet hole (4) is formed outside the controllable flocculation device (1), and a stirring motor (5) is arranged outside the controllable flocculation device (1); the overlaid spiral sludge dehydrating machine (8) comprises a dehydrating system, a swimming ring (9), a fixed ring (10) and a driving motor A (15); and a sludge feeding hole (18) is formed at the upper side of one end of the gear type sludge dehydrating drying machine (25), a sludge discharging hole (19) is formed at the lower side of the other end of the gear type sludge dehydrating drying machine (25), a solvent steam exhaust hole (21) is formed at the upper end of the gear type sludge dehydrating drying machine (25), a condensed water tank (26) is arranged at the lower end of the gear type sludge dehydrating drying machine (25), and the air purifying system (23) is arranged on the solvent steam exhaust hole (21).
Description
Technical field
The utility model relates to the environmental protection equipment field, more precisely the integrated deep dehydration desiccation machine of a kind of mud.
Background technology
The sludge dehydrating and drying of prior art is divided into dehydration and two technologies of mummification and equipment to be handled, at first sewage is passed through water extracter, pressure filter or other dehydration equipments drop to about 80% the water ratio of mud after handling, need lot of manpower and material resources to transport to handle the laggard next procedure of going into then, or landfill or purchase huge anhydration system and carry out drying and other treatment, time consumption and energy consumption, cost of idleness, clearly proposing sludge moisture content in country's 12 planning must be reduced to about 40%, this has just brought programmatic guide for existing sludge dewatering, therefore, at this requirement, work out both energy-saving consumption-reducings, easy to use again, the integrated deep dehydration desiccation machine of mud that more meets national industrial policies has been trend of the times.
The utility model content
The purpose of this utility model is to overcome above-mentioned weak point, and a kind of easy to use, save energy is provided, the integrated deep dehydration desiccation machine of mud that diversification is used.
The utility model for achieving the above object, by the following technical solutions: the integrated deep dehydration desiccation machine of a kind of mud, it comprises controllable type flocculation plant, full-automatic electrical control system, folded spiral shell formula sludge dewatering equipment, gear type mud dryer and air-purification system, the inside of described controllable type flocculation plant is provided with liquidometer, overflow spout and flocculation tempering tank, and the outside is provided with sewage admission port and agitator motor; Described folded spiral shell formula sludge dewatering equipment comprises dewatering system, the ring that moves about, set collar and drive-motor A, wherein, described dewatering system is made up of enriching section, extruded segment and dewatering period three parts, described ring and the set collar of moving about is located in the cavity of folded spiral shell formula sludge dewatering equipment, and described drive-motor A is located at an end of screw shaft spindle nose in the folded spiral shell formula sludge dewatering equipment; The upside that described gear type mud takes off desiccation machine one end is provided with sludge inlet, the downside of the other end is provided with the sludge-drying discharge port, the upper end is provided with the solvent vapo(u)r relief outlet, the lower end is provided with condensation water tank, inner parallel placement gear type spiral impeller-hub, the right-hand member of gear type spiral impeller-hub and condensation water tank is provided with the heat-conducting medium entrance, left end is provided with the heat-conducting medium outlet, outer setting has full-automatic electrical control system, full-automatic electrical control system is provided with automatic temperature control system, and described solvent vapo(u)r relief outlet is provided with air-purification system.
Described controllable type flocculation plant is connected with the mud inlet of folded spiral shell formula sludge dewatering equipment.
The airtight connection of sludge inlet of the mud mouth of described folded spiral shell formula sludge dewatering equipment and gear type sludge drying machine, and the junction is provided with the automatic open close baffle plate.
The left end of described gear type sludge drying machine is provided with drive-motor B.
Described gear type spiral impeller-hub is hollow shape.
Described heat-conducting medium entrance comprises heat-conducting medium entrance A and heat-conducting medium entrance B.
Described heat-conducting medium outlet comprises heat-conducting medium outlet A and heat-conducting medium outlet B.
In the utility model, the controllable type flocculation plant is installed in the front end of folded spiral shell formula sludge dewatering equipment, be connected with the mud inlet of folded spiral shell formula sludge dewatering equipment, enter the body of folded spiral shell formula sludge dewatering equipment, carry out the dehydration of mud, the mud of dehydration back water ratio about 80% enters full-automatic transport pipe by mud mouth, this pipeline is connected with the mud inlet of gear type mud dryer, the cavity that mud enters gear type mud dryer is dried, and under the promotion of gear type screw shaft, constantly advance to the sludge-drying discharge port, the solvent vapo(u)r that produces in mud drying process enters and is back to sewage lagoon after condensation water tank cools off, and gas can directly discharge after entering air-purification system.
The utlity model has multiple function and purposes, can be according to different wherein one or both forms that share, the compact constructions of adopting separately with kind of former concentration of hydraulic mixture, the integrated degree height, sludge treatment effect stability, less energy-consumption, maintenance is little, totally-enclosed operation, non-secondary pollution.
The beneficial effects of the utility model are in particular in:
1, the utility model links up into a total workflow with mud from flocculation, dehydration, mummification, the integrated degree height makes compact overall structure, and saves cost and drop into and working cost, thoroughly solve the handling problem of mud, reached the purpose of decrement, harmless processing.
2, the utility model is provided with two place's heat-conducting medium entrances, the heat transfer area maximization, and rate of drying is faster.
3, gear type spiral impeller-hub of the present utility model is compact to design rationally, and at the uniform velocity rotation can make mud evenly be stirred, and dry dynamics is even; Use geartransmission power, have characteristics such as compact construction, efficient height, life-span length, save energy.
4, the utility model is provided with the automatic open close baffle plate in the sludge inlet of gear type sludge drying machine, can prevent effectively that heat runs off, and plays the effect of save energy.
5, the utility model is provided with full-automatic control system, need not manual operation, simple and fast.
6, the utility model is provided with condensation water tank, effectively reduces potential safety hazard; And condensation water tank is connected with sewage lagoon, form the workflow of a smoothness, need not manual operation, more saved water.
7, the utility model is provided with air-purification system, can make the toxic and harmful of discharging in the sludge handling process through emission abatement, can not cause secondary pollution.
8, gear type sludge drying machine of the present utility model is provided with automatic temperature control system, and the control of mummification temperature in 250 ℃, had both been prevented problems such as the too high energy consumption that causes of temperature is excessive, potential safety hazard, has guaranteed the best calorific value of excess sludge again.
Description of drawings
Below in conjunction with accompanying drawing the utility model is further elaborated.
Fig. 1 is the structural representation among the utility model embodiment.
Among the figure: 1, controllable type flocculation plant; 2, liquidometer; 3, overflow spout; 4, sewage admission port; 5, agitator motor; 6, flocculation tempering tank; 7, mud inlet; 8, folded spiral shell formula sludge dewatering equipment; 9, the ring that moves about; 10, set collar; 11, enriching section; 12, extruded segment; 13, dewatering period; 14, mud mouth; 15, drive-motor A; 16, heat-conducting medium entrance; The outlet of 17 heat-conducting mediums; 18, sludge inlet; 19, sludge-drying discharge port; 20, gear type spiral impeller-hub; 21, solvent vapo(u)r relief outlet; 22, automatic open close baffle plate; 23, air-purification system; 24, drive-motor B; 25, gear type sludge drying machine; 26, condensation water tank; 27, automatic temperature control system.
Specific implementation method:
The integrated deep dehydration desiccation machine of a kind of mud as shown in Figure 1, it comprises controllable type flocculation plant 1, full-automatic electrical control system, folded spiral shell formula sludge dewatering equipment 8, gear type mud dryer 25 and air-purification system 23, the inside of described controllable type flocculation plant 1 is provided with liquidometer 2, overflow spout 3 and flocculation tempering tank 6, and the outside is provided with sewage admission port 4 and agitator motor 5; Described folded spiral shell formula sludge dewatering equipment 8 comprises dewatering system, ring 9, set collar 10 and drive-motor A15 move about, wherein, described dewatering system is made up of enriching section 11, extruded segment 12 and dewatering period 13 3 parts, described ring 9 and the set collar 10 of moving about is located in the cavity of folded spiral shell formula sludge dewatering equipment 8, and described drive-motor A15 is located at an end of screw shaft spindle nose in the folded spiral shell formula sludge dewatering equipment 8; The upside that described gear type mud takes off desiccation machine 25 1 ends is provided with sludge inlet 18, the downside of the other end is provided with sludge-drying discharge port 19, the upper end is provided with solvent vapo(u)r relief outlet 21, the lower end is provided with condensation water tank 26, inner parallel placement gear type spiral impeller-hub 20, the right-hand member of gear type spiral impeller-hub 20 and condensation water tank 26 is provided with heat-conducting medium entrance 16, left end is provided with heat-conducting medium outlet 17, outer setting has full-automatic electrical control system, full-automatic electrical control system is provided with automatic temperature control system 27, and described solvent vapo(u)r relief outlet 21 is provided with air-purification system 23.
Described controllable type flocculation plant 1 is connected with the mud inlet 7 of folded spiral shell formula sludge dewatering equipment 8.
18 airtight connections of sludge inlet of the mud mouth 14 of described folded spiral shell formula sludge dewatering equipment 8 and gear type sludge drying machine 25, and the junction is provided with automatic open close baffle plate 22.
The left end of described gear type sludge drying machine 25 is provided with drive-motor B24.
Described gear type spiral impeller-hub 20 is hollow shape.
Described heat-conducting medium entrance 16 comprises heat-conducting medium entrance A and heat-conducting medium entrance B.
Described heat-conducting medium outlet 17 comprises heat-conducting medium outlet A and heat-conducting medium outlet B.
The utility model enters into flocculation tempering tank 6 at sewage from sewage admission port 4, flocculate under the stirring of agitator motor 5 mix into floc sedimentation after, enter the mud inlet 7 of folded spiral shell formula sludge dewatering equipment 8, in controllable type flocculation plant 1, be provided with liquidometer 2, when liquid level reaches set(ting)value, can flow into overflow spout 3; The sewage that flocculation is good flows into the cavity of folded spiral shell formula sludge dewatering equipment 8 from mud inlet 7, cavity by one group or the multiple set collar 10 of having organized intussusception and the ring 9 and be provided with drive-motor A15 at spindle nose and form of moving about more, through enriching section 11, enter extruded segment 12, arriving dewatering period 13 at last dewaters, dehydration back water ratio enters airtight and is provided with the sludge inlet 18 of automatic open close baffle plate 22 from mud mouth 14 at the mud cake below 80%, enter gear type sludge drying machine 25, its heat-conducting medium carries out circulating heat conduction from the heat-conducting medium entrance B two that the spindle nose of an end heat-conducting medium entrance A of gear type sludge drying machine 25 and gear type spiral impeller-hub 20 is provided with, make the heat transfer area maximization, rate of drying is faster, and cooled heat-conducting medium is discharged from heat-conducting medium outlet A and heat-conducting medium outlet B; Above gear type sludge drying machine 25, be provided with solvent vapo(u)r relief outlet 21, the flux steam of discharging enters condensation water tank 26 by pipeline and cools off, directly enter sewage lagoon after the water temperature of condensation water tank 26 reaches design temperature, gas enters air-purification system 23 and purifies directly discharging of back; Under the at the uniform velocity promotion of gear type spiral impeller-hub 20, being heated of mud is more balanced, farthest avoided the mud adhesion problems, oven dry back water ratio becomes small bulk at the mud below 40%, enter sludge-drying discharge port 19, finished from the integrated workflow of flocculation, dehydration, oven dry; Whole working cycle is provided with full-automatic control system, need not manual operation.
Principle of work of the present utility model and flow process are: turn on the power switch, after sewage enters controllable type flocculation plant 1 and flocculates from sewage admission port 4, enter the cavity of folded spiral shell formula sludge dewatering equipment 8 from the mud inlet 7 of folded spiral shell formula sludge dewatering equipment 8, through enriching section 11, extruded segment 12, dewatering period 13 dewaters, dehydration back water ratio at the mud cake 80% below from folding spiral shell formula sludge dewatering equipment 8 mud mouths 14 and enter airtight and being provided with the sludge inlet 18 of automatic open close baffle plate 22, enter the cavity of the gear type sludge drying machine 25 that is provided with two place's heat-conducting medium entrances 16, heat-conducting medium in the gear type sludge drying machine 25 enters in cavity and the gear type spiral impeller-hub 20, temperature constantly raises, mud is constantly pushed ahead by gear type spiral impeller-hub 20 uniformly from sludge inlet 18, make being heated of mud more balanced, circulating heat conduction through heat-conducting medium, the water ratio of mud constantly descends, the water ratio of mud can be down to about 40% when arriving sludge-drying discharge port 19, realized the purpose of sludge drying, the water vapour that produces in the mud drying process enters air-purification system 23 from the solvent vapo(u)r mouth relief outlet 21 of top, discharges after purifying.
The utility model is at first through the screw extrusion dehydration with sewage, carry out a novel sludge treatment device that the know-why of degree of depth mummification is designed by hollow wheel gear and cavity circulating heat conduction then, be widely used in wide field such as municipal wastewater, oil refinery, printing and dyeing, papermaking, coalification, ore dressing, biochemistry, pharmacy, food, sugaring, leather, carry out technological innovation with save energy, simple to operate, theory such as be widely used, can adapt to the requirement of different industries, and for using enterprise to save a large amount of operation costs.
The utility model is the indispensable equipment of sewage treatment project, mud after treatment can be made material of construction, be processed into mud powder making cement stopping composition or exploitation gac substitute, contain can also refining of noble metal, can also do nuisanceless processing such as farmland fertilizer or landfill, can not cause secondary pollution to environment.
The utility model can separately use according to customer demand, also can form a complete system, has farthest satisfied the requirement of client for sludge treatment.
The utility model has been realized the integrated progress of work of sludge dewatering to mummification, realizes less energy-consumption, high-level efficiency in equipment running process, and automatically need not special messenger guard's operational mode.
Claims (7)
1. integrated deep dehydration desiccation machine of mud, it comprises controllable type flocculation plant (1), full-automatic electrical control system, folded spiral shell formula sludge dewatering equipment (8), gear type mud dryer (25) and air-purification system (23), it is characterized in that: the inside of described controllable type flocculation plant (1) is provided with liquidometer (2), overflow spout (3) and flocculation tempering tank (6), and the outside is provided with sewage admission port (4) and agitator motor (5); Described folded spiral shell formula sludge dewatering equipment (8) comprises dewatering system, the ring (9) that moves about, set collar (10) and drive-motor A(15), wherein, described dewatering system is made up of enriching section (11), extruded segment (12) and dewatering period (13) three parts, described move about ring (9) and set collar (10) are located in the cavity of folded spiral shell formula sludge dewatering equipment (8), described drive-motor A(15) be located at an end of screw shaft spindle nose in the folded spiral shell formula sludge dewatering equipment (8); The upside that described gear type mud takes off desiccation machine (25) one ends is provided with sludge inlet (18), the downside of the other end is provided with sludge-drying discharge port (19), the upper end is provided with solvent vapo(u)r relief outlet (21), the lower end is provided with condensation water tank (26), inner parallel placement gear type spiral impeller-hub (20), the right-hand member of gear type spiral impeller-hub (20) and condensation water tank (26) is provided with heat-conducting medium entrance (16), left end is provided with heat-conducting medium outlet (17), outer setting has full-automatic electrical control system, full-automatic electrical control system is provided with automatic temperature control system (27), and described solvent vapo(u)r relief outlet (21) is provided with air-purification system (23).
2. by the integrated deep dehydration desiccation machine of the described a kind of mud of claim 1, it is characterized in that: described controllable type flocculation plant (1) is connected with the mud inlet (7) of folded spiral shell formula sludge dewatering equipment (8).
3. by the integrated deep dehydration desiccation machine of the described a kind of mud of claim 1, it is characterized in that: the mud mouth (14) of described folded spiral shell formula sludge dewatering equipment (8) and airtight connection of sludge inlet (18) of gear type sludge drying machine (25), and the junction is provided with automatic open close baffle plate (22).
4. by the integrated deep dehydration desiccation machine of the described a kind of mud of claim 1, it is characterized in that: the left end of described gear type sludge drying machine (25) is provided with drive-motor B(24).
5. by the integrated deep dehydration desiccation machine of the described a kind of mud of claim 1, it is characterized in that: described gear type spiral impeller-hub (20) is hollow shape.
6. by the integrated deep dehydration desiccation machine of the described a kind of mud of claim 1, it is characterized in that: described heat-conducting medium entrance (16) comprises heat-conducting medium entrance A and heat-conducting medium entrance B.
7. by the integrated deep dehydration desiccation machine of the described a kind of mud of claim 1, it is characterized in that: described heat-conducting medium outlet (17) comprises heat-conducting medium outlet A and heat-conducting medium outlet B.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320100970 CN203128381U (en) | 2013-03-06 | 2013-03-06 | Integrated sludge deep dehydrating drying machine |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320100970 CN203128381U (en) | 2013-03-06 | 2013-03-06 | Integrated sludge deep dehydrating drying machine |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203128381U true CN203128381U (en) | 2013-08-14 |
Family
ID=48936379
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320100970 Expired - Fee Related CN203128381U (en) | 2013-03-06 | 2013-03-06 | Integrated sludge deep dehydrating drying machine |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203128381U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103588376A (en) * | 2013-11-20 | 2014-02-19 | 泰州市蓝海环保科技有限公司 | Gear type sludge dryer |
| CN103833198A (en) * | 2013-03-06 | 2014-06-04 | 泰州市蓝海环保科技有限公司 | Sludge integrated deep dewatering dryer |
| CN106116093A (en) * | 2016-07-22 | 2016-11-16 | 浙江双林机械股份有限公司 | Sludge dehydrating and drying machine and dehydration and drying method |
| CN107540188A (en) * | 2017-09-27 | 2018-01-05 | 杨沁玥 | A kind of high efficiency spiral sludge dewatering machine |
| CN108862815A (en) * | 2018-05-25 | 2018-11-23 | 张玉峰 | Dry-wet separation sewage treatment device |
-
2013
- 2013-03-06 CN CN 201320100970 patent/CN203128381U/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103833198A (en) * | 2013-03-06 | 2014-06-04 | 泰州市蓝海环保科技有限公司 | Sludge integrated deep dewatering dryer |
| CN103588376A (en) * | 2013-11-20 | 2014-02-19 | 泰州市蓝海环保科技有限公司 | Gear type sludge dryer |
| CN106116093A (en) * | 2016-07-22 | 2016-11-16 | 浙江双林机械股份有限公司 | Sludge dehydrating and drying machine and dehydration and drying method |
| CN106116093B (en) * | 2016-07-22 | 2019-03-26 | 浙江双林机械股份有限公司 | Sludge dehydrating and drying machine and dehydration and drying method |
| CN107540188A (en) * | 2017-09-27 | 2018-01-05 | 杨沁玥 | A kind of high efficiency spiral sludge dewatering machine |
| CN108862815A (en) * | 2018-05-25 | 2018-11-23 | 张玉峰 | Dry-wet separation sewage treatment device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203128381U (en) | Integrated sludge deep dehydrating drying machine | |
| CN103833198A (en) | Sludge integrated deep dewatering dryer | |
| CN105417923A (en) | Sludge drying system | |
| CN101823829A (en) | Extrusion sludge dewatering system | |
| CN201686602U (en) | Extrusion type sludge dewatering system | |
| CN204689863U (en) | A kind of sludge condensation division box and system | |
| CN206244582U (en) | Dyeing and printing sewage processing system | |
| JP7003192B1 (en) | Organic sludge treatment equipment and treatment method | |
| CN204824568U (en) | Mud decrement processing system | |
| CN204588967U (en) | A kind of novel sludge drier | |
| CN103588376A (en) | Gear type sludge dryer | |
| CN203866169U (en) | Rotary type sludge filter | |
| CN203602478U (en) | Rotary extrusion type sludge dryer | |
| CN202297339U (en) | Sludge drying treatment system | |
| CN203602475U (en) | Dryer suitable for sludge dewatering | |
| CN203602479U (en) | Novel sludge dryer | |
| CN104649549A (en) | Full-automatic sludge drier | |
| CN203602477U (en) | Safe sludge dryer | |
| CN104649557A (en) | Automatic sludge drier | |
| CN204874162U (en) | Add fever type industrial wastewater treatment equipment | |
| CN203602474U (en) | Novel efficient sludge dryer | |
| CN204981568U (en) | Centrifugal sludge dewatering system | |
| CN204417305U (en) | A kind of high speed sludge treating system | |
| CN213113018U (en) | Continuous sludge dewatering mummification system | |
| CN104649538A (en) | A rotating extrusion type sludge dewatering machine |
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: 20130814 Termination date: 20170306 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |