CN201678473U - Continuous alkylate wastewater treatment device - Google Patents
Continuous alkylate wastewater treatment device Download PDFInfo
- Publication number
- CN201678473U CN201678473U CN2010201917053U CN201020191705U CN201678473U CN 201678473 U CN201678473 U CN 201678473U CN 2010201917053 U CN2010201917053 U CN 2010201917053U CN 201020191705 U CN201020191705 U CN 201020191705U CN 201678473 U CN201678473 U CN 201678473U
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- Prior art keywords
- graphite
- wastewater treatment
- continuous
- alkylate
- hydrochloric acid
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
A continuous alkylate wastewater treatment device consists of an organic heat carrier furnace (1), a heat conduction oil circulation pump (2), a slicer (4), a rotor flow meter (5), a hydrochloric acid receiving tank (6) and a high-level wastewater tank (8). The continuous alkylate wastewater treatment device is characterized in that the heat conduction oil circulation lamp (2) is connected with a side wall of the lower end of a graphite cylindrical block evaporator (3), a side wall of the upper end of the graphite cylindrical block evaporator (3) is connected with the slicer (4) through a pipeline, the top end of the graphite cylindrical block evaporator (3) is connected to one end of a graphite condenser (7) through a pipeline, and the other end of the graphite condenser (7) is connected with the hydrochloric acid receiving tank (6). Therefore, the continuous alkylate wastewater treatment device is reasonable in design, can effectively realize continuous production, is long in service life, resists high temperature, corrosion and cold and hot impact, and is particularly suitable for wastewater treatment.
Description
Technical field:
The utility model relates to a kind of wastewater treatment equipment, particularly a kind of continous way alkylation wastewater treatment equipment.
Background technology:
At present, China is when the Chemical Manufacture alkylated reaction, hydrochloric and magnesium chloride waste water by Grignard reagent reaction generation, need handle, general processing mode is with thermal oil circulation heating glassed steel reaction vessels, after moisture and hydrochloric acid are removed in evaporation, cooling generates the magnesium chloride hexahydrate solid, interrupter method is handled, because the cold-resistant thermal shocking of glassed steel reaction vessels is poor, glass-lined coating very easily produces the burst porcelain phenomenon, and contain hydrochloric acid in the waste water, produce hydrogen-type corrosion after the burst porcelain, glassed steel reaction vessels is scrapped, service life of equipment is shorter.
Summary of the invention:
The utility model be exactly to provide a kind of equipment design rationally, can realize effectively that continuous production, service life of equipment are long, high temperature resistant, corrosion-resistant, the wastewater treatment equipment of cold-resistant thermal shocking.
The purpose of this utility model is achieved in that a kind of continous way alkylation wastewater treatment equipment, by organic heat carrier furnace, the thermal oil recycle pump, slicing machine, spinner-type flowmeter, the hydrochloric acid receiving tank, the waste water high level tank is formed, it is characterized in that being connected on the lower end sidewall of described thermal oil recycle pump by pipeline and graphite nahlock hole vaporizer, be connected with described slicing machine by pipeline on the sidewall of vaporizer upper end, graphite nahlock hole, the top of graphite nahlock hole vaporizer is by an end of pipe connection graphite condenser, and the other end of graphite condenser is connected with described hydrochloric acid receiving tank.
The utility model compared with prior art has the following advantages:
Be connected owing to adopt on the lower end sidewall of thermal oil recycle pump by pipeline and graphite nahlock hole vaporizer, be connected with described slicing machine by pipeline on the sidewall of vaporizer upper end, graphite nahlock hole, the top of graphite nahlock hole vaporizer is by an end of pipe connection graphite condenser, the other end of graphite condenser and described hydrochloric acid are accepted tank connected structure formation, thereby equipment design is reasonable, can effectively realize continuous production, long, high temperature resistant, corrosion-resistant, the cold-resistant thermal shocking of service life of equipment.
Description of drawings:
Figure: be the utility model concrete structure synoptic diagram.
1, organic heat carrier furnace 2, thermal oil recycle pump 3, graphite nahlock hole vaporizer 4, slicing machine 5, spinner-type flowmeter 6, hydrochloric acid receiving tank 7, graphite condenser 8, waste water high level tank
Embodiment:
Organic heat carrier furnace 1, thermal oil recycle pump 2, slicing machine 4, spinner-type flowmeter 5, hydrochloric acid receiving tank 6, waste water high level tank 8 adopt existing structure formation and shape, just be connected on the lower end sidewall by pipeline and graphite nahlock hole vaporizer 3 on the thermal oil recycle pump 2, be connected with slicing machine 4 by pipeline on the sidewall of vaporizer 3 upper ends, graphite nahlock hole, the top of graphite nahlock hole vaporizer 3 is by an end of pipe connection graphite condenser 7, and the other end of graphite condenser is connected with hydrochloric acid receiving tank 7
During use, waste water changes waste water high level tank 8 over to, the turn-on flow rate variable valve, be full of graphite nahlock hole vaporizer 3 in advance, start thermal oil recycle pump 2, organic heat carrier furnace 1 heats up and keeps design temperature, observe spinner-type flowmeter 5 and regulate flow, the high-temp chlorination magnesium of output is made the halogen sheet through slicing machine 4 coolings, enters into hydrochloric acid receiving tank 6, recycling through containing of graphite nahlock hole vaporizer 3 evaporations the hydrogenchloride water vapor forms hydrochloric acid after graphite condenser 7 cools off after.
Claims (1)
1. continous way alkylation wastewater treatment equipment, by organic heat carrier furnace (1), thermal oil recycle pump (2), slicing machine (4), spinner-type flowmeter (5), hydrochloric acid receiving tank (6), waste water high level tank (8) is formed, it is characterized in that being connected on the lower end sidewall of described thermal oil recycle pump (2) by pipeline and graphite nahlock hole vaporizer (3), be connected with described slicing machine (4) by pipeline on the sidewall of graphite nahlock hole vaporizer (3) upper end, the top of graphite nahlock hole vaporizer (3) is by an end of pipe connection graphite condenser (7), and the other end of graphite condenser (7) is connected with described hydrochloric acid receiving tank (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201917053U CN201678473U (en) | 2010-05-06 | 2010-05-06 | Continuous alkylate wastewater treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010201917053U CN201678473U (en) | 2010-05-06 | 2010-05-06 | Continuous alkylate wastewater treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201678473U true CN201678473U (en) | 2010-12-22 |
Family
ID=43343526
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010201917053U Expired - Fee Related CN201678473U (en) | 2010-05-06 | 2010-05-06 | Continuous alkylate wastewater treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201678473U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105700007A (en) * | 2016-04-08 | 2016-06-22 | 江苏省核与辐射安全监督管理局 | Radioactive water sample evaporation and concentration device and method |
-
2010
- 2010-05-06 CN CN2010201917053U patent/CN201678473U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105700007A (en) * | 2016-04-08 | 2016-06-22 | 江苏省核与辐射安全监督管理局 | Radioactive water sample evaporation and concentration device and method |
| CN105700007B (en) * | 2016-04-08 | 2018-12-25 | 江苏省核与辐射安全监督管理局 | A kind of radioactivity water sample evaporation concentration device and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20101222 Termination date: 20110506 |