CN209368074U - A kind of sludge drying system for the production of triazine axoplasm - Google Patents
A kind of sludge drying system for the production of triazine axoplasm Download PDFInfo
- Publication number
- CN209368074U CN209368074U CN201822157484.7U CN201822157484U CN209368074U CN 209368074 U CN209368074 U CN 209368074U CN 201822157484 U CN201822157484 U CN 201822157484U CN 209368074 U CN209368074 U CN 209368074U
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- Prior art keywords
- sludge
- spiral shell
- machine
- folds
- shell machine
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- 239000010802 sludge Substances 0.000 title claims abstract description 47
- 238000001035 drying Methods 0.000 title claims abstract description 11
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 10
- JYEUMXHLPRZUAT-UHFFFAOYSA-N 1,2,3-triazine Chemical compound C1=CN=NN=C1 JYEUMXHLPRZUAT-UHFFFAOYSA-N 0.000 title claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000428 dust Substances 0.000 claims abstract description 13
- 238000001816 cooling Methods 0.000 claims abstract description 9
- 239000007788 liquid Substances 0.000 claims abstract description 7
- 239000000463 material Substances 0.000 claims abstract description 6
- 239000010865 sewage Substances 0.000 claims abstract description 6
- 239000007787 solid Substances 0.000 claims abstract description 6
- 230000008676 import Effects 0.000 claims abstract description 4
- 238000000034 method Methods 0.000 description 9
- 238000003825 pressing Methods 0.000 description 6
- 239000002351 wastewater Substances 0.000 description 5
- 239000002910 solid waste Substances 0.000 description 3
- 238000004806 packaging method and process Methods 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000001939 inductive effect Effects 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses a kind of sludge drying systems for the production of triazine axoplasm, it includes sludge and folds spiral shell machine, the top inlet that sludge folds spiral shell machine connects Fenton, biochemical sludge liquid pump, the overflow port that sludge folds spiral shell machine connects Fenton kettle, the bottom that sludge folds spiral shell machine connects sewage collecting pool, sludge folds spiral shell machine and connects feeding spiral conveyer, the import of feeding spiral conveyer is also connected with board and frame machine, feeding spiral conveyer is connected with hollow blade dryer, the dry material of hollow blade dryer discharge enters charging cooling spiral conveyer, it feeds cooling spiral conveyer and carries out solids package, the tail gas of hollow blade dryer discharge enters water dust scrubber, the gas outlet of water dust scrubber is connected with air-introduced machine, air-introduced machine is connect with chimney, water dust scrubber is connected with water circulating pump.The utility model reduces the workload manually packed, and sludge total amount after desiccation is dehydrated reduces 50%, saved Treatment of Sludge cost.
Description
Technical field
The utility model relates to a kind of sludge drying systems for the production of triazine axoplasm.
Background technique
After having waste water output, this strand of waste water to carry out Fenton filters pressing in triazine axoplasm production process, liquid portion enters life
Change system is handled, and the solid isolated carries out big packaging bag.Original filters pressing is carried out plus is filtered using sheet frame, this operation needs people
Work feeds filters pressing, and dismantles and need to shovel material pack manually, and labor workload is larger.Because water content is higher in solid, output
Solid waste amount is larger, and processing cost is high.
Summary of the invention
The purpose of this utility model is to overcome above deficiency, provide it is a kind of reduce the workload manually packed,
The sludge drying system for the production of triazine axoplasm of Treatment of Sludge cost is saved.
The purpose of this utility model is achieved through the following technical solutions: a kind of sludge drying for the production of triazine axoplasm
System, including sludge fold spiral shell machine, and the top inlet that sludge folds spiral shell machine connects Fenton, biochemical sludge liquid pump, and sludge folds overflowing for spiral shell machine
Head piece connects Fenton kettle, and the bottom that sludge folds spiral shell machine connects sewage collecting pool, and sludge folds spiral shell machine and connects feeding spiral conveyer, into
The import of material screw conveyor is also connected with board and frame machine, and feeding spiral conveyer is connected with hollow blade dryer, hollow blade
The dry material of drying machine discharge enters charging cooling spiral conveyer, and charging cooling spiral conveyer carries out solids package, hollow
The tail gas of blade dryer discharge enters water dust scrubber, and the gas outlet of water dust scrubber is connected with air-introduced machine, air-introduced machine and cigarette
Chimney connection, water dust scrubber are connected with water circulating pump.
Compared with the prior art, the utility model has the following advantages: the utility model passes through the solution after waste water Fenton
Pump enters back into folded spiral shell press filteration system after squeezing into head tank, enters back into drying system after folded spiral shell filters pressing, realizes continuous feed, dry
Sludge afterwards directly packs.The utility model reduces the workload manually packed.Through counting, sludge total amount after desiccation is dehydrated
Reduce 50%, has saved Treatment of Sludge cost.
Detailed description of the invention:
Fig. 1 is the structural schematic diagram of the utility model；
Figure label: 1- sludge fold spiral shell machine, 2- Fenton, biochemical sludge liquid pump, 3- Fenton kettle, 4- sewage collecting pool,
5- feeding spiral conveyer, 6- board and frame machine, 7- hollow blade dryer, 8- feed cooling spiral conveyer, 9- water film dedusting
Device, 10- air-introduced machine, 11- chimney, 12- water circulating pump.
Specific embodiment:
It, below will be to the utility model to keep the objectives, technical solutions, and advantages of the embodiments of the present invention clearer
Technical solution in embodiment is clearly and completely described, it is clear that described embodiment is that the utility model a part is real
Example is applied, instead of all the embodiments.The elements and features described in a kind of embodiment of the utility model can be with one
Elements and features shown in a or more other embodiment combine.It should be noted that for purposes of clarity, in explanation
The expression and description of component unrelated with the utility model, known to persons of ordinary skill in the art and processing is omitted.It is based on
The embodiments of the present invention, those of ordinary skill in the art institute obtained under the premise of not making the creative labor
There are other embodiments, fall within the protection scope of the utility model.
A kind of a kind of embodiment party of the sludge drying system for the production of triazine axoplasm of the utility model as shown in figure 1
Formula, including sludge fold spiral shell machine 1, and the top inlet that sludge folds spiral shell machine 1 connects Fenton, biochemical sludge liquid pump 2, and sludge folds spiral shell machine 1
Overflow port connects Fenton kettle 3, and the bottom that sludge folds spiral shell machine 1 connects sewage collecting pool 4, and it is defeated that sludge folds the connection of spiral shell machine 1 feed auger
Machine 5 is sent, the import of feeding spiral conveyer 5 is also connected with board and frame machine 6, and it is dry that feeding spiral conveyer 5 is connected with hollow blade
Machine 7, hollow blade dryer 7 be discharged dry material enter charging cooling spiral conveyer 8, charging cooling spiral conveyer 8 into
Row solids package, the tail gas that hollow blade dryer 7 is discharged enter water dust scrubber 9, the gas outlet of water dust scrubber 9 and air inducing
Machine 10 is connected, and air-introduced machine 10 is connect with chimney 11, and water dust scrubber 9 is connected with water circulating pump 12.
By the organic wastewater containing high concentration generated in manufacture process by pump convey into Fenton's reaction kettle into
Row Fenton's reaction；The sludge after mud waste water and biochemistry after reaction is squeezed by Fenton, biochemical sludge liquid pump 2 later
Sludge folds spiral shell machine 1 and carries out filters pressing, and filtrate enters sewage collecting pool 4, and filter residue enters hopper, to be dried；Sludge after filters pressing is logical
Feeding spiral conveyer 5 is crossed to be dried into hollow blade dryer 7；Sludge after drying carries out big packaging weighing and send solid waste
Stockyard, tail gas enter water dust scrubber 9 and carry out out dirt, and the tail gas after dirt passes through 10 row of air-introduced machine to chimney 11 out.
The utility model improves operating environment, reduces sludge solid waste total amount to optimize sludge press filtration technique.
Wherein, the basic parameter of the folded spiral shell machine of sludge and design condition are as follows:
The basic parameter of hollow blade dryer and design condition are as follows:
Finally, it should be noted that although the utility model and its advantage have been described in detail above it should be appreciated that
Various change can be carried out without departing from the spirit and scope of the utility model being defined by the claims appended hereto
Become, substitute and converts.Moreover, the scope of the utility model is not limited only to process, equipment described in specification, means, method
With the specific embodiment of step.One of ordinary skilled in the art is from the disclosure of the utility model it will be readily understood that root
It can be used according to the utility model and execute the function of communicating substantially to corresponding embodiment described herein or obtain basic with it
The result communicated, existing and to be developed in the future process, equipment, means, method or step.Therefore, appended right
It is required that be intended to includes such process, equipment, means, method or step in the range of them.
Claims (1)
1. a kind of sludge drying system for the production of triazine axoplasm, it is characterised in that: fold spiral shell machine (1), the dirt including sludge
The top inlet that mud folds spiral shell machine (1) connects Fenton, biochemical sludge liquid pump (2), and the overflow port that the sludge folds spiral shell machine (1) connects fragrant
Pause kettle (3), the bottom that the sludge folds spiral shell machine (1) connects sewage collecting pool (4), and the sludge folds spiral shell machine (1) connection and feeds spiral shell
It revolves conveyer (5), the import of the feeding spiral conveyer (5) is also connected with board and frame machine (6), the feeding spiral conveyer
(5) it is connected with hollow blade dryer (7), the dry material of hollow blade dryer (7) discharge enters charging cooling spiral
Conveyer (8), the charging cooling spiral conveyer (8) carry out solids package, the tail of hollow blade dryer (7) discharge
Gas enters water dust scrubber (9), and the gas outlet of the water dust scrubber (9) is connected with air-introduced machine (10), the air-introduced machine (10)
It is connect with chimney (11), the water dust scrubber (9) is connected with water circulating pump (12).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822157484.7U CN209368074U (en) | 2018-12-21 | 2018-12-21 | A kind of sludge drying system for the production of triazine axoplasm |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822157484.7U CN209368074U (en) | 2018-12-21 | 2018-12-21 | A kind of sludge drying system for the production of triazine axoplasm |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209368074U true CN209368074U (en) | 2019-09-10 |
Family
ID=67829849
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822157484.7U Active CN209368074U (en) | 2018-12-21 | 2018-12-21 | A kind of sludge drying system for the production of triazine axoplasm |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209368074U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116282823A (en) * | 2023-03-21 | 2023-06-23 | 江苏博尔科环保科技有限公司 | A convective sludge granulation drying system |
-
2018
- 2018-12-21 CN CN201822157484.7U patent/CN209368074U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116282823A (en) * | 2023-03-21 | 2023-06-23 | 江苏博尔科环保科技有限公司 | A convective sludge granulation drying system |
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