CN205020059U - Production system of naphthenate - Google Patents
Production system of naphthenate Download PDFInfo
- Publication number
- CN205020059U CN205020059U CN201520687856.0U CN201520687856U CN205020059U CN 205020059 U CN205020059 U CN 205020059U CN 201520687856 U CN201520687856 U CN 201520687856U CN 205020059 U CN205020059 U CN 205020059U
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- China
- Prior art keywords
- tank
- pipeline
- purifying column
- condenser
- naphthenate
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Abstract
The utility model discloses a production system of naphthenate, including reaction kettle system, exhaust gas purification system and sewage purification system, reaction kettle system include support frame, vacuum pump, vacuum buffer tank, metering tank, reation kettle body, condenser, storage tank and the pump body one, reation kettle body fixed mounting on the support frame, other pipe connection metering tank in reation kettle's top and condenser, the vacuum buffer tank is connected to the vacuum -pump line, vacuum buffer tank and metering tank pipe connection, and the storage tank is connected to the condenser pipeline, and the storage tank passes through the pipe connection pump body no. 1, exhaust gas purification system includes purifying column and atomizing device, and the lower part and the condenser pipeline of purifying column are connected, and the upper portion of purifying column is provided with the clean air export, and the external pump body of purifying column two, the pump body no. 2 and atomizing device pipe connection, the problem of current naphthenate production cause that environmental pollution ecological unbalance and pipeline are direct to be added the raw materials to reation kettle and cause the wasting of resources and the increasing of the subsequent processing degree of difficulty is solved.
Description
Technical field
The utility model relates to technical field of chemical production equipment, is specifically related to a kind of production system of naphthenate.
Background technology
Along with the development of society, country is more and more higher to environmental requirement, and the equipment of existing production naphthenate mostly only enters air or surface pond after one purified treatment, process not thorough, environmental pollution destroys serious, causes disruption of ecological balance, does not meet the requirement of current sustainable development view; The equipment of existing production naphthenate is mostly directly add in reactor body by pipeline, add speed and addition wayward, cause reaction insufficient, cause the wasting of resources and subsequent treatment difficulty to strengthen.
Utility model content
For solving the problems of the technologies described above, we have proposed a kind of production system of naphthenate, discharge after solving existing naphthenate production equipment waste water and gas primary purification and cause environmental pollution disruption of ecological balance and pipeline to add raw material interpolation speed and the wayward problem causing the wasting of resources and subsequent treatment difficulty to strengthen of addition directly to reactor.
For solving the problem, the technical solution of the utility model is as follows:
A kind of production system of naphthenate, comprise reactor system, waste gas cleaning system and sewage purification system, described reactor system comprises bracing frame, vavuum pump, vacuum buffer tank, measuring tank, reactor body, condenser, storage tank and the pump housing one, described reactor body is fixedly installed on support frame as described above, and the upper part of described reactor body be don't bother about road and connected described measuring tank and condenser; Described vacuum-pump line connects described vacuum buffer tank, and described vacuum buffer tank is connected with described measuring tank pipeline, and described condenser tubes connects described storage tank, and described storage tank connects the described pump housing one by pipeline;
Described waste gas cleaning system comprises purifying column, atomising device, chemicals dosing plant and water tank, the bottom of described purifying column is connected with described condenser tubes, the top of described purifying column is provided with clean air outlet, the external pump housing two of described purifying column, the described pump housing two is connected with described atomising device pipeline, described atomising device is connected with described chemicals dosing plant pipeline, and described atomising device is also connected with described water tank pipeline;
Described sewage purification system comprises PAM dissolving tank, mixer one, PAC dissolving tank, mixer two, regulating reservoir, flotation tank, intermediate pool, sandfiltration pot and sludge drying pond, described regulating reservoir is connected with the bottom pipe of described purifying column, described regulating reservoir is provided with described PAC dissolving tank, described PAC dissolves in pipe and installs described mixer two, described regulating reservoir is connected with described flotation tank pipeline, described PAM dissolving tank is installed on described mixer one on described flotation tank and is installed on described PAM dissolving tank, described flotation tank respectively pipeline connects described intermediate pool and sludge drying pond, described intermediate pool pipeline connects described sandfiltration pot, described sandfiltration pot pipeline connects described sludge drying pond, described sludge drying pond pipeline connects described regulating reservoir.
Preferably, described storage tank is provided with four, is arranged side by side about four described storage tanks.
Pass through technique scheme, the production system of a kind of naphthenate that the utility model proposes, by arranging reactor system, waste gas cleaning system and sewage purification system, discharging after solving existing naphthenate production equipment waste water and gas primary purification and causing environmental pollution disruption of ecological balance and pipeline to add raw material interpolation speed and the wayward problem causing the wasting of resources and subsequent treatment difficulty to strengthen of addition directly to reactor.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the block architecture diagram schematic diagram of the production system of a kind of naphthenate disclosed in the utility model embodiment;
Fig. 2 is the sectional perspective structural representation of the reactor system of the production system of a kind of naphthenate disclosed in the utility model embodiment;
Fig. 3 is the perspective view of the waste gas cleaning system of the production system of a kind of naphthenate disclosed in the utility model embodiment;
Fig. 4 is the perspective view of the sewage purification system of the production system of a kind of naphthenate disclosed in the utility model embodiment.
Numeral and the corresponding component title represented by letter in figure:
1. reactor system 2. waste gas cleaning system 3. sewage purification system
11. bracing frame 12. vavuum pump 13. vacuum buffer tanks
14. measuring tank 15. reactor body 16. condensers
17. storage tank 18. pump housing 1 purifying columns
22. atomising device 23. chemicals dosing plant 24. water tanks
25. pump housing two 31.PAM dissolving tank 32. mixers one
33.PAC dissolving tank 34. mixer 2 35. regulating reservoir
36. flotation tank 37. intermediate pool 38. sandfiltration pots
39. sludge drying ponds.
Detailed description of the invention
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Below in conjunction with embodiment and detailed description of the invention, the utility model is described in further detail.
Embodiment
As shown in Figure 1, a kind of production system of naphthenate, comprise reactor system 1, waste gas cleaning system 2 and sewage purification system 3, described reactor system 1 comprises bracing frame 11, vavuum pump 12, vacuum buffer tank 13, measuring tank 14, reactor body 15, condenser 16, storage tank 17 and the pump housing 1, described reactor body 15 is fixedly installed on support frame as described above 11, and the upper part of described reactor body 15 be don't bother about road and connected described measuring tank 14 and condenser 16; Described vavuum pump 12 pipeline connects described vacuum buffer tank 13, and described vacuum buffer tank 13 is connected with described measuring tank 14 pipeline, and described condenser 16 pipeline connects described storage tank 17, and described storage tank 17 connects the described pump housing 1 by pipeline;
Described waste gas cleaning system 2 comprises purifying column 21, atomising device 22, chemicals dosing plant 23 and water tank 24, the bottom of described purifying column 21 is connected with described condenser 16 pipeline, the top of described purifying column 21 is provided with clean air outlet, the external pump housing 2 25 of described purifying column 21, the described pump housing 2 25 is connected with described atomising device 22 pipeline, described atomising device 22 is connected with described chemicals dosing plant 23 pipeline, and described atomising device 22 is also connected with described water tank 24 pipeline;
Described sewage purification system 3 comprises PAM dissolving tank 31, mixer 1, PAC dissolving tank 33, mixer 2 34, regulating reservoir 35, flotation tank 36, intermediate pool 37, sandfiltration pot 38 and sludge drying pond 39, described regulating reservoir 35 is connected with the bottom pipe of described purifying column 21, described regulating reservoir 35 is provided with described PAC dissolving tank 33, described PAC dissolves in pipe and installs described mixer 2 34, described regulating reservoir 35 is connected with described flotation tank 36 pipeline, described PAM dissolving tank 31 is installed on described mixer 1 on described flotation tank 36 and is installed on described PAM dissolving tank 31, described flotation tank 36 respectively pipeline connects described intermediate pool 37 and sludge drying pond 39, described intermediate pool 37 pipeline connects described sandfiltration pot 38, described sandfiltration pot 38 pipeline connects described sludge drying pond 39, described sludge drying pond 39 pipeline connects described regulating reservoir 35.
Described storage tank 17 is provided with four, and four described storage tanks about 17 are arranged side by side.
Pass through technique scheme, the production system of a kind of naphthenate that the utility model proposes, by arranging reactor system 1, waste gas cleaning system 2 and sewage purification system 3, discharging after solving existing naphthenate production equipment waste water and gas primary purification and causing environmental pollution disruption of ecological balance and pipeline to add raw material interpolation speed and the wayward problem causing the wasting of resources and subsequent treatment difficulty to strengthen of addition directly to reactor.
Above-described is only the preferred embodiment of the production system of a kind of naphthenate of the utility model; should be understood that; for the person of ordinary skill of the art; under the prerequisite not departing from the utility model creation design; can also make some distortion and improvement, these all belong to protection domain of the present utility model.
Claims (2)
1. the production system of a naphthenate, it is characterized in that, comprise reactor system, waste gas cleaning system and sewage purification system, described reactor system comprises bracing frame, vavuum pump, vacuum buffer tank, measuring tank, reactor body, condenser, storage tank and the pump housing one, described reactor body is fixedly installed on support frame as described above, and the upper part of described reactor body be don't bother about road and connected described measuring tank and condenser; Described vacuum-pump line connects described vacuum buffer tank, and described vacuum buffer tank is connected with described measuring tank pipeline, and described condenser tubes connects described storage tank, and described storage tank connects the described pump housing one by pipeline;
Described waste gas cleaning system comprises purifying column, atomising device, chemicals dosing plant and water tank, the bottom of described purifying column is connected with described condenser tubes, the top of described purifying column is provided with clean air outlet, the external pump housing two of described purifying column, the described pump housing two is connected with described atomising device pipeline, described atomising device is connected with described chemicals dosing plant pipeline, and described atomising device is also connected with described water tank pipeline;
Described sewage purification system comprises PAM dissolving tank, mixer one, PAC dissolving tank, mixer two, regulating reservoir, flotation tank, intermediate pool, sandfiltration pot and sludge drying pond, described regulating reservoir is connected with the bottom pipe of described purifying column, described regulating reservoir is provided with described PAC dissolving tank, described PAC dissolves in pipe and installs described mixer two, described regulating reservoir is connected with described flotation tank pipeline, described PAM dissolving tank is installed on described mixer one on described flotation tank and is installed on described PAM dissolving tank, described flotation tank respectively pipeline connects described intermediate pool and sludge drying pond, described intermediate pool pipeline connects described sandfiltration pot, described sandfiltration pot pipeline connects described sludge drying pond, described sludge drying pond pipeline connects described regulating reservoir.
2. the production system of a kind of naphthenate according to claim 1, is characterized in that, described storage tank is provided with four, is arranged side by side about four described storage tanks.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520687856.0U CN205020059U (en) | 2015-09-07 | 2015-09-07 | Production system of naphthenate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520687856.0U CN205020059U (en) | 2015-09-07 | 2015-09-07 | Production system of naphthenate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205020059U true CN205020059U (en) | 2016-02-10 |
Family
ID=55252627
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520687856.0U Expired - Fee Related CN205020059U (en) | 2015-09-07 | 2015-09-07 | Production system of naphthenate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205020059U (en) |
-
2015
- 2015-09-07 CN CN201520687856.0U patent/CN205020059U/en not_active Expired - Fee Related
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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: 20160210 Termination date: 20160907 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |