CN205056011U - Production system of inhibition anti -tartar agent - Google Patents
Production system of inhibition anti -tartar agent Download PDFInfo
- Publication number
- CN205056011U CN205056011U CN201520765883.5U CN201520765883U CN205056011U CN 205056011 U CN205056011 U CN 205056011U CN 201520765883 U CN201520765883 U CN 201520765883U CN 205056011 U CN205056011 U CN 205056011U
- Authority
- CN
- China
- Prior art keywords
- reation kettle
- reactor
- production system
- batch
- feed inlet
- 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
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The utility model relates to a production system of inhibition anti -tartar agent, it includes a reation kettle, the 2nd reation kettle and settling cask, they link to each other through the pipeline the inside agitating unit that all is equipped with of a reation kettle and the 2nd reation kettle a reation kettle upper portion is equipped with feed inlet I and condensation port a reation kettle lower part inboard is equipped with steam heating pipe reation kettle bottom inboard is equipped with the nitrogen gas coil pipe of giving vent to anger, feed inlet I links to each other with the material jar be equipped with the automatic blending ware between feed inlet I and the material jar, condensation port links to each other with the condenser the 2nd reation kettle upper portion is equipped with feed inlet II the settling cask lower part is equipped with the discharge gate the settling cask bottom is equipped with the baiting valve. The utility model discloses automatic batching, the product yield is high, wholly moves safe and reliable, environmental protection.
Description
Technical field
The utility model relates to a kind of production system, is specifically related to a kind of production system of antitartar agents.
Background technology
A lot of oil plant finds, when after the fouling of hydrogenation high pressure air cooling, the fractionator overhead condensations such as oil plant Atmospheric vacuum, catalytic cracking, hydrocracking, hydrodesulfurization, low-temperature level produce dew point corrosion, threaten the safety in production of device, also can bring the rising of pressure drop simultaneously, the treating capacity of device is declined.
Summary of the invention
Goal of the invention: the purpose of this utility model is that provide a kind of automatic proportioning, product yield is high, and overall operation is safe and reliable in order to overcome deficiency of the prior art, the production system of the inhibition antitartar agents of environmental protection.
Technical scheme: in order to solve the problems of the technologies described above, the production system of a kind of inhibition antitartar agents described in the utility model, it comprises the first reactor, second reactor and settling tank, they are connected by pipeline, all agitating device is provided with at described first reactor and the second reactor inside, charging aperture I and condensate port is provided with on described first reactor top, steam-heating pipe is provided with in described first reactor lower inside, be provided with nitrogen in described first reactor bottom inside and go out gas coil pipe, described charging aperture I is connected with batch can, autoproportioner is provided with between described charging aperture I and batch can, described condensate port is connected with condenser, charging aperture II is provided with on described second reactor top, discharging opening is provided with in described settling tank bottom, baiting valve is provided with bottom described settling tank.
Described batch can is divided into the first batch can and the second batch can, and they are all connected with autoproportioner respectively.
Be connected with condensate liquid collection groove bottom described condenser.
Baiting valve bottom described settling tank is connected with autoproportioner by pipeline.
Beneficial effect: compared with prior art, its remarkable advantage is the utility model: the utility model adopts the first reactor and condenser, and steam-heating pipe is set in the first reactor and nitrogen goes out gas coil pipe, ensure high yield, adopt settling tank, pass through natural sedimentation, ensure product purity, adopt autoproportioner, realize automation, whole installation is reasonable, Matter Transfer utilizes, and operates steadily safe and reliable, pollution-free in whole production process, environmental protection, realistic instructions for use.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Detailed description of the invention
Below in conjunction with drawings and Examples, the utility model is further described.
As shown in Figure 1, the production system of a kind of inhibition antitartar agents described in the utility model, it comprises the first reactor 1, second reactor 2 and settling tank 3, they are connected by pipeline, agitating device 4 is all provided with at described first reactor 1 and the second reactor 2 inside, charging aperture I 5 and condensate port 6 is provided with on described first reactor 1 top, steam-heating pipe 7 is provided with in described first reactor 1 lower inside, be provided with nitrogen in described first reactor 1 bottom inside and go out gas coil pipe 8, described charging aperture I 5 is connected with batch can, autoproportioner 9 is provided with between described charging aperture I 5 and batch can, described condensate port 6 is connected with condenser 10, charging aperture II 11 is provided with on described second reactor 2 top, discharging opening 12 is provided with in described settling tank 3 bottom, baiting valve 13 is provided with bottom described settling tank 3, described batch can is divided into the first batch can 14 and the second batch can 15, and they are all connected with autoproportioner 9 respectively, be connected with condensate liquid collection groove 16 bottom described condenser 10, baiting valve 13 bottom described settling tank 3 is connected with autoproportioner 9 by pipeline.The utility model adopts the first reactor and condenser, and in the first reactor, arranges steam-heating pipe and nitrogen goes out gas coil pipe, ensures high yield, adopt settling tank, by natural sedimentation, ensure product purity, adopt autoproportioner, realize automation, whole installation is reasonable, and Matter Transfer utilizes, operate steadily safe and reliable, pollution-free in whole production process, environmental protection, realistic instructions for use.
The utility model provides a kind of thinking and method; the method and access of this technical scheme of specific implementation is a lot; the above is only preferred embodiment of the present utility model; should be understood that; for those skilled in the art, under the prerequisite not departing from the utility model principle, some improvements and modifications can also be made; these improvements and modifications also should be considered as protection domain of the present utility model, and all available prior art of each part not clear and definite in the present embodiment is realized.
Claims (4)
1. the production system of an inhibition antitartar agents, it is characterized in that: it comprises the first reactor (1), second reactor (2) and settling tank (3), they are connected by pipeline, agitating device (4) is all provided with described first reactor (1) and the second reactor (2) inside, charging aperture I (5) and condensate port (6) is provided with on described first reactor (1) top, steam-heating pipe (7) is provided with in described first reactor (1) lower inside, be provided with nitrogen in described first reactor (1) bottom inside and go out gas coil pipe (8), described charging aperture I (5) is connected with batch can, autoproportioner (9) is provided with between described charging aperture I (5) and batch can, described condensate port (6) is connected with condenser (10), charging aperture II (11) is provided with on described second reactor (2) top, discharging opening (12) is provided with in described settling tank (3) bottom, baiting valve (13) is provided with in described settling tank (3) bottom.
2. the production system of inhibition antitartar agents according to claim 1, is characterized in that: described batch can is divided into the first batch can (14) and the second batch can (15), and they are all connected with autoproportioner (9) respectively.
3. the production system of inhibition antitartar agents according to claim 1, is characterized in that: described condenser (10) bottom is connected with condensate liquid collection groove (16).
4. the production system of inhibition antitartar agents according to claim 1, is characterized in that: the baiting valve (13) of described settling tank (3) bottom is connected with autoproportioner (9) by pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520765883.5U CN205056011U (en) | 2015-09-30 | 2015-09-30 | Production system of inhibition anti -tartar agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520765883.5U CN205056011U (en) | 2015-09-30 | 2015-09-30 | Production system of inhibition anti -tartar agent |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205056011U true CN205056011U (en) | 2016-03-02 |
Family
ID=55382615
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520765883.5U Expired - Fee Related CN205056011U (en) | 2015-09-30 | 2015-09-30 | Production system of inhibition anti -tartar agent |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205056011U (en) |
-
2015
- 2015-09-30 CN CN201520765883.5U patent/CN205056011U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN205368255U (en) | Semicontinuous device of mink cell focus lightization in overcritical solvent environment | |
| CN201625192U (en) | Integrated control system for preparing traditional Chinese medicine extracts | |
| CN205056011U (en) | Production system of inhibition anti -tartar agent | |
| CN202018832U (en) | Test device for loss of coolant accident (LOCA) of nuclear power station | |
| CN204154563U (en) | PTA Equipment oxidation reaction tail gas on-line checkingi sample gas pretreating system | |
| CN203043795U (en) | Coking decoking waste gas treatment device | |
| CN203030013U (en) | Solvent recovery and water removal device for sucralose production | |
| CN205164708U (en) | Production system of residual oil detersive for hydrogenated apparatus;hydrogenated unit | |
| CN211346401U (en) | Vacuum low-temperature dehydration equipment | |
| CN106552563A (en) | A kind of production system of inhibition antitartar agents | |
| CN203479046U (en) | Device for recycling condensate steam in process of production | |
| CN106563404A (en) | Production system for detergent for residue oil hydrotreating device | |
| CN203558989U (en) | Extraction system for polyoxymethylene dimethyl ether preparation device | |
| CN103585785B (en) | Drying device and method for triethylamine in production process of glyphosate | |
| CN105061134A (en) | Method and device for separating high-purity longifolene | |
| CN205042440U (en) | With amine liquid recovery system of corrosion inhibitor in composite | |
| CN204778907U (en) | Evaporation plant who handles coking desulfurization waste liquid is exclusively used in | |
| CN204665955U (en) | The cold broken preheater of a kind of liquid material | |
| CN203803132U (en) | Combined solvent deacidification, dechlorination and deamination equipment | |
| CN205055466U (en) | Ester type anti -wear agent molecule rectification plant | |
| CN218130093U (en) | 2-chlorine-5-chloromethyl thiazole acid extraction and waste acid processing apparatus in succession | |
| CN204320044U (en) | Fermentation tank tail gas spray system | |
| CN204380294U (en) | For easily producing the distilling apparatus of corrosive gas | |
| CN211562437U (en) | Butyraldehyde, octenal hydrogenation catalyst passivation gas processing apparatus | |
| CN209778379U (en) | Oil-water separating device |
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: 20160302 Termination date: 20200930 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |