CN106563404A - Production system for detergent for residue oil hydrotreating device - Google Patents
Production system for detergent for residue oil hydrotreating device Download PDFInfo
- Publication number
- CN106563404A CN106563404A CN201510653445.4A CN201510653445A CN106563404A CN 106563404 A CN106563404 A CN 106563404A CN 201510653445 A CN201510653445 A CN 201510653445A CN 106563404 A CN106563404 A CN 106563404A
- Authority
- CN
- China
- Prior art keywords
- reactor
- production system
- reaction kettle
- batch
- condenser
- 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
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention relates to a production system for detergent for a residue oil hydrotreating device. The production system comprises a first reaction kettle and a second reaction kettle. A nitrogen outlet pipe is arranged on the inner side of the bottom of the first reaction kettle. A heating pipe is arranged on the inner side of the lower portion of the first reaction kettle. One side of the upper portion of the first reaction kettle is provided with a feed inlet I. The other side of the upper portion of the first reaction kettle is provided with a condensation opening. The feed inlet I is connected with a material tank. An automatic batcher is arranged between the feed inlet I and the material tank. The condensation opening is connected with a condenser I. A condenser II is arranged on a pipeline between the first reaction kettle and the second reaction kettle. The upper portion of the second reaction kettle is provided with a charging opening II. The bottom of the second reaction kettle is provided with a discharge outlet. The production system achieves automation, the water content is qualified, and environmental protection and safety are achieved.
Description
Technical field
The present invention relates to a kind of production system, and in particular to a kind of detersive production system.
Background technology
In recent years, due to the continuous heaviness of refinery feedstock, the fouling, coking problem in oil refining process on equipment becomes increasingly conspicuous.Decline and affect unit normal run this problem to solve hydrocracking unit heat exchanger heat exchange efficiency, have developed residuum hydrodesulfurization device detersive.The production system of existing residual oil detersive arranges unreasonable, fluctuation of service, low production efficiency, the risk for having secondary pollution.
The content of the invention
Goal of the invention：The invention aims to overcome deficiency of the prior art, there is provided a kind of automatization, water content is qualified, environmental protection, the production system of the residual hydrogenation equipment detersive of safety.
Technical scheme：In order to solve above-mentioned technical problem, a kind of production system of residual hydrogenation equipment detersive of the present invention, it includes the first reactor and the second reactor, they are connected by pipeline, agitating device is designed with first reactor and the second reactor, nitrogen out of the trachea is provided with the inside of first reactor bottom, heating tube is provided with the first reactor lower inside, charging aperture I is provided with the first reactor top side, opposite side is provided with condensate port, the charging aperture I is connected with batch can, autoproportioner is provided between the charging aperture I and batch can, the condensate port is connected with condenser I, condenser II is provided with pipeline between first reactor and the second reactor, charge door II is provided with the second reactor top, second reactor bottom is provided with discharging opening.
The batch can is divided into the first batch can and the second batch can, and they are all connected respectively with autoproportioner.
The bottom of the condenser I is connected with condensed fluid collection groove.
The heating tube is heat-conducting oil pipes.
Second reactor bottom is connected with charging basket.
Beneficial effect：Compared with prior art, its remarkable advantage is the present invention：Whole installation of the present invention rationally, is used cooperatively using the first reactor and condenser I, and product yield is high, using heating tube and nitrogen out of the trachea, excessive moisture is taken out of by nitrogen, it is ensured that product water content is qualified, and operate steadily, safe and reliable, material passes through autoproportioner, accurately in place, automatization is realized, using condenser II, make the temperature of charge in the second reactor at 40 DEG C or so, facilitate barrelling, it is pollution-free in production process, environmental protection, meets actual operation requirements.
Description of the drawings
Fig. 1 is the structural representation of the present invention.
Specific embodiment
With reference to the accompanying drawings and examples the present invention is further illustrated.
As shown in Figure 1，A kind of production system of residual hydrogenation equipment detersive of the present invention，It includes the first reactor 1 and the second reactor 2，They are connected by pipeline，Agitating device 3 is designed with the reactor 2 of first reactor 1 and second，Nitrogen out of the trachea 4 is provided with the bottom inside of the first reactor 1，Heating tube 5 is provided with the lower inside of the first reactor 1，Charging aperture I 6 is provided with the top side of first reactor 1，Opposite side is provided with condensate port 7，The charging aperture I 6 is connected with batch can，Autoproportioner 8 is provided between the charging aperture I 6 and batch can，The condensate port 7 is connected with condenser I 9，Condenser II 10 is provided with pipeline between the reactor 2 of first reactor 1 and second，Charge door II 11 is provided with the top of the second reactor 2，The bottom of second reactor 2 is provided with discharging opening 12；The batch can is divided into the first batch can 13 and the second batch can 14, and they are all connected respectively with autoproportioner 8；The bottom of the condenser I 9 is connected with condensed fluid collection groove 15；The heating tube 5 is heat-conducting oil pipes；The bottom of second reactor 2 is connected with charging basket 16.Whole installation of the present invention rationally, is used cooperatively using the first reactor and condenser I, and product yield is high, using heating tube and nitrogen out of the trachea, excessive moisture is taken out of by nitrogen, it is ensured that product water content is qualified, and operate steadily, safe and reliable, material passes through autoproportioner, accurately in place, automatization is realized, using condenser II, make the temperature of charge in the second reactor at 40 DEG C or so, facilitate barrelling, it is pollution-free in production process, environmental protection, meets actual operation requirements.
The invention provides a kind of thinking and method; the method and approach for implementing the technical scheme is a lot; the above is only the preferred embodiment of the present invention; it should be understood that; for those skilled in the art, under the premise without departing from the principles of the invention, some improvements and modifications can also be made; these improvements and modifications also should be regarded as protection scope of the present invention, and clearly each ingredient not can use prior art to be realized in the present embodiment.
Claims (5)
1. a kind of production system of residual hydrogenation equipment detersive, it is characterised in that：It includes the first reactor（1）With the second reactor（2）, they are connected by pipeline, in first reactor（1）With the second reactor（2）Inside it is designed with agitating device（3）, in first reactor（1）Bottom inside is provided with nitrogen out of the trachea（4）, in first reactor（1）Lower inside is provided with heating tube（5）, in first reactor（1）Top side is provided with charging aperture I（6）, opposite side is provided with condensate port（7）, the charging aperture I（6）It is connected with batch can, in the charging aperture I（6）Autoproportioner is provided with and batch can between（8）, the condensate port（7）With condenser I（9）It is connected, in first reactor（1）With the second reactor（2）Between pipeline be provided with condenser II（10）, in second reactor（2）Top is provided with charge door II（11）, second reactor（2）Bottom is provided with discharging opening（12）.
2. the production system of residual hydrogenation equipment detersive according to claim 1, it is characterised in that：The batch can is divided into the first batch can（13）With the second batch can（14）, they respectively all with autoproportioner（8）It is connected.
3. the production system of residual hydrogenation equipment detersive according to claim 1, it is characterised in that：The condenser I（9）Bottom and condensed fluid collection groove（15）It is connected.
4. the production system of residual hydrogenation equipment detersive according to claim 1, it is characterised in that：The heating tube（5）For heat-conducting oil pipes.
5. the production system of residual hydrogenation equipment detersive according to claim 1, it is characterised in that：Second reactor（2）Bottom and charging basket（16）It is connected.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510653445.4A CN106563404A (en) | 2015-10-12 | 2015-10-12 | Production system for detergent for residue oil hydrotreating device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510653445.4A CN106563404A (en) | 2015-10-12 | 2015-10-12 | Production system for detergent for residue oil hydrotreating device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106563404A true CN106563404A (en) | 2017-04-19 |
Family
ID=58506764
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510653445.4A Pending CN106563404A (en) | 2015-10-12 | 2015-10-12 | Production system for detergent for residue oil hydrotreating device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106563404A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110292899A (en) * | 2019-04-19 | 2019-10-01 | 东南大学 | High temperature microwave reaction kettle combined apparatus and reaction method |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202295379U (en) * | 2011-09-28 | 2012-07-04 | 郑州正力聚合物科技有限公司 | Inflating pipe for bagging and packing polyacrylamide |
| CN204320269U (en) * | 2014-12-09 | 2015-05-13 | 西安联控电气有限责任公司 | A kind of production of resins line reaction unit |
| CN104830362A (en) * | 2015-05-13 | 2015-08-12 | 武汉科技大学 | Manufacturing technique of industrial binder asphalt |
-
2015
- 2015-10-12 CN CN201510653445.4A patent/CN106563404A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN202295379U (en) * | 2011-09-28 | 2012-07-04 | 郑州正力聚合物科技有限公司 | Inflating pipe for bagging and packing polyacrylamide |
| CN204320269U (en) * | 2014-12-09 | 2015-05-13 | 西安联控电气有限责任公司 | A kind of production of resins line reaction unit |
| CN104830362A (en) * | 2015-05-13 | 2015-08-12 | 武汉科技大学 | Manufacturing technique of industrial binder asphalt |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110292899A (en) * | 2019-04-19 | 2019-10-01 | 东南大学 | High temperature microwave reaction kettle combined apparatus and reaction method |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202214306U (en) | Process device for preparing ethanol by utilizing acetic acid | |
| CN103933923A (en) | Continuous reaction production line consisting of multiple serially connected reaction kettles | |
| CN106398724A (en) | Waste heat recovery device for ascending pipe of coke oven | |
| CN205368255U (en) | Semi-continuous device for lightening heavy oil in supercritical solvent environment | |
| CN207347520U (en) | A kind of system of diesel hydrotreating unit naphtha direct-furnish reformer | |
| CN106563404A (en) | Production system for detergent for residue oil hydrotreating device | |
| CN109603376A (en) | A kind of high-temperature oil gas of waste and old rubber thermal cracking and carbon black separation system | |
| CN110482494B (en) | Energy-saving continuous sulfur melting process without waste liquid discharge | |
| CN115975664A (en) | Delayed coking coke tower heat control process | |
| CN205164708U (en) | Production system of residual oil detersive for hydrogenated apparatus;hydrogenated unit | |
| CN204153760U (en) | A kind of waste hot steam waste-heat recovery device | |
| CN103601626B (en) | A kind of methyl cyclopentenyl ketone resets stepwise reaction method | |
| CN106479668B (en) | Device for extracting star anise oil by negative pressure circulating water | |
| CN205227896U (en) | Condensate water is recovery system again | |
| CN205056011U (en) | Production system of inhibition anti -tartar agent | |
| CN201710986U (en) | Pressure-reducing and deep-drawing distiller | |
| CN203620636U (en) | Easily heated polycondensation reaction kettle | |
| CN204778907U (en) | Evaporation plant who handles coking desulfurization waste liquid is exclusively used in | |
| CN105013407A (en) | Organic fluorination reaction kettle device | |
| CN203866252U (en) | Double-pipe flow guide center feeding structure for full-automatic bottom cover machine | |
| CN108607231B (en) | Rectifying device and rectifying method | |
| CN205228237U (en) | Take soda plate heat exchanger of desuperrheater | |
| CN104593064B (en) | The separation method of pyrolysis gasoline hydrogenation device second stage reactor outlet material | |
| CN203990562U (en) | Many the new type of continuous reaction production lines that reactor is composed in series | |
| CN211471311U (en) | Fine fractionation device for hydrogenation process |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| RJ01 | Rejection of invention patent application after publication | ||
| RJ01 | Rejection of invention patent application after publication |
Application publication date: 20170419 |