CN205119874U - Petrifaction oil refining is cooling device for coker - Google Patents
Petrifaction oil refining is cooling device for coker Download PDFInfo
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- CN205119874U CN205119874U CN201520779290.4U CN201520779290U CN205119874U CN 205119874 U CN205119874 U CN 205119874U CN 201520779290 U CN201520779290 U CN 201520779290U CN 205119874 U CN205119874 U CN 205119874U
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- high temperature
- temperature resistant
- cooling box
- circulating
- condensed water
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Abstract
The utility model discloses a petrifaction oil refining is cooling device for coker, go into pipe, comdenstion water circulation tank and delivery pipe including gas, water connection, the bottom that upper strata table lid that the pipe penetrability passed high temperature resistant cooling box stretched into high temperature resistant cooling box is gone into to gas, water connection, and the delivery pipe setting is at the top of high temperature resistant cooling box, comdenstion water circulation tank installs in the bottom of high temperature resistant cooling box, and is connected with circulating condensate pipe on comdenstion water circulation tank's the upper surface, the right side of high temperature resistant cooling box is provided with the drain valve. The utility model has the advantages of being scientific and reasonable in structure, adopt circulating condensate pipe, not only make the cooling effect show more, add unnecessary vapor, convenient subsequent processing and processing can for moreover the tail gas after the cooling, the right side is provided with the drain valve, makes things convenient for the staff to open the drain valve when using for a long time, drives inside relict moisture, its life of effectual extension.
Description
Technical field
The utility model belongs to high temperature cooling technique field, is specifically related to a kind of petrochemical refining coking plant cooling device.
Background technology
In order to promote industrial expansion, petro-chemical corporation keeps away unavoidable socially, the emission before the discharging of the coke produced by its coking plant has fatal impact for the living environment of people, it has, the undesirable element such as impulsive force large, heat high, smell large, be difficult to centralized collection and distribute scope wide large containing cinder amount, cause the solution that petro-chemical corporation has not had this yet, direct discharge can not reach its environmental requirement certainly, will cause environmental disruption, and affect healthy series of problems of Denging.
If want, its emission is processed, high temperature is the first operation needing to overcome, therefore cooling device is absolutely necessary, existing cooling device, mostly adopts the mode of spray to lower the temperature, this mode not only cooling effectiveness is low, and easily cause the doping of a large amount of steam in tail gas, for follow-up process and purification increase burden, inner long-term the contact with water of device can not get regular maintenance, Long-Time Service will have a strong impact on its service life, increases user's financial burden.These problems be all hinder petrochemical industry development the most important thing, need our solve.
Utility model content
The purpose of this utility model is to provide a kind of petrochemical refining coking plant cooling device, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme: a kind of petrochemical refining coking plant cooling device, comprise gas, water access tube, high temperature resistant cooling box, circulating condensate pipe, condensed water circulating water tank and delivery pipe, described gas, water access tube penetrability extend into the bottom of high temperature resistant cooling box through the upper strata table cover of high temperature resistant cooling box, and delivery pipe is arranged on the top of high temperature resistant cooling box, described condensed water circulating water tank is arranged on the bottom of high temperature resistant cooling box, and the upper surface of condensed water circulating water tank is connected with circulating condensate pipe, the right side of described high temperature resistant cooling box is provided with draining valve.
Preferably, described condensed water circulating water tank is made up of the stand-by storehouse of condensed water, circulating water condensing case and circulation conduit.
Preferably, the left end of described circulating condensate pipe embeds and is connected on the upper surface in the stand-by storehouse of condensed water, and right-hand member embeds and is connected on the upper surface of circulating water condensing case.
Compared with prior art, the beneficial effects of the utility model are: this petrochemical refining's coking plant cooling device is scientific and reasonable for structure, safe and convenient to use, break existing spraying cooling mode, adopt circulating condensate pipe, not only make cooling-down effect more remarkable, and increase unnecessary steam, convenient follow-up processing and process can not to the tail gas after cooling; Condensed water circulating water tank is made up of the stand-by storehouse of condensed water, circulating water condensing case and circulation conduit, and itself and circulating condensate pipe cooperatively interact work, achieve recycling of condensed water, reduces cost of investment, alleviates the financial burden of user; Right side is provided with draining valve, facilitates staff to open draining valve during Long-Time Service, removes the moisture of internal residual, effectively extends its service life.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
Fig. 2 is condensed water circulating water tank structural representation of the present utility model.
In figure: 1, gas, water access tube, 2, high temperature resistant cooling box, 3, circulating condensate pipe, 4, condensed water circulating water tank, 41, the stand-by storehouse of condensed water, 42, circulating water condensing case, 43, circulation conduit, 5, delivery pipe, 6, draining valve.
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.
Refer to Fig. 1-2, the utility model provides a kind of technical scheme: a kind of petrochemical refining coking plant cooling device, comprise gas, water access tube 1, high temperature resistant cooling box 2, circulating condensate pipe 3, condensed water circulating water tank 4 and delivery pipe 5, gas, water access tube 1 penetrability extend into the bottom of high temperature resistant cooling box 2 through the upper strata table cover of high temperature resistant cooling box 2, and delivery pipe 5 is arranged on the top of high temperature resistant cooling box 2, condensed water circulating water tank 4 is arranged on the bottom of high temperature resistant cooling box 2, and the upper surface of condensed water circulating water tank 4 is connected with circulating condensate pipe 3, condensed water circulating water tank 4 is by the stand-by storehouse 41 of condensed water, circulating water condensing case 42 and circulation conduit 43 form, the left end of circulating condensate pipe 3 embeds and is connected on the upper surface in the stand-by storehouse 41 of condensed water, right-hand member embeds and is connected on the upper surface of circulating water condensing case 42, the right side of high temperature resistant cooling box 2 is provided with draining valve 6.
Operation principle: convenience and high-efficiency when the utility model uses, first the emission of petrochemical refining's coking plant is after simple filtration, directly pass through gas, water access tube 1 imports the inside of high temperature resistant cooling box 2, waste gas floats because its density is less, circulating condensate pipe 3 adopts the principle of air conditioner refrigerating, heat contained in efficient absorption waste gas, condensed water absorbs heat, reach the object of waste gas cooling, successful tail gas of finally lowering the temperature is discharged by the delivery pipe 5 at top, enter next treating apparatus, condensed water after absorption heat is under the guiding of circulating condensate pipe 3, flow into circulating water condensing case 42 and carry out reducing temperature twice, the stand-by storehouse 41 of condensed water is again flowed into eventually through circulation conduit 43, the secondary achieving condensed water utilizes, the stable of condensed water in condensed water circulating water tank 4 is maintained while reducing costs, right side is provided with draining valve 6, staff is facilitated to open draining valve 6 during Long-Time Service, remove the moisture of internal residual, effective prolongation its service life.
Although illustrate and described embodiment of the present utility model, for the ordinary skill in the art, be appreciated that and can carry out multiple change, amendment, replacement and modification to these embodiments when not departing from principle of the present utility model and spirit, scope of the present utility model is by claims and equivalents thereof.
Claims (3)
1. petrochemical refining's coking plant cooling device, comprise gas, water access tube (1), high temperature resistant cooling box (2), circulating condensate pipe (3), condensed water circulating water tank (4) and delivery pipe (5), it is characterized in that: described gas, water access tube (1) penetrability extend into the bottom of high temperature resistant cooling box (2) through the upper strata table cover of high temperature resistant cooling box (2), and delivery pipe (5) is arranged on the top of high temperature resistant cooling box (2), described condensed water circulating water tank (4) is arranged on the bottom of high temperature resistant cooling box (2), and the upper surface of condensed water circulating water tank (4) is connected with circulating condensate pipe (3), the right side of described high temperature resistant cooling box (2) is provided with draining valve (6).
2. a kind of petrochemical refining according to claim 1 coking plant cooling device, is characterized in that: described condensed water circulating water tank (4) is made up of the stand-by storehouse of condensed water (41), circulating water condensing case (42) and circulation conduit (43).
3. a kind of petrochemical refining according to claim 1 and 2 coking plant cooling device, it is characterized in that: the left end of described circulating condensate pipe (3) embeds and is connected on the upper surface in the stand-by storehouse of condensed water (41), and right-hand member embeds and is connected on the upper surface of circulating water condensing case (42).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520779290.4U CN205119874U (en) | 2015-10-09 | 2015-10-09 | Petrifaction oil refining is cooling device for coker |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520779290.4U CN205119874U (en) | 2015-10-09 | 2015-10-09 | Petrifaction oil refining is cooling device for coker |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205119874U true CN205119874U (en) | 2016-03-30 |
Family
ID=55575475
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520779290.4U Expired - Fee Related CN205119874U (en) | 2015-10-09 | 2015-10-09 | Petrifaction oil refining is cooling device for coker |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205119874U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106838956A (en) * | 2017-01-13 | 2017-06-13 | 安徽未名鼎和环保有限公司 | A kind of refuse burner exhaust gas processing device |
| CN107914343A (en) * | 2017-11-30 | 2018-04-17 | 双钱集团（江苏）轮胎有限公司 | A kind of new temperature control device for Banbury mixer |
| CN108592491A (en) * | 2018-04-24 | 2018-09-28 | 河南龙丰实业股份有限公司 | The inorganic refrigerated energy-saving down cycles system of culture medium of edible fungus cooling chamber |
-
2015
- 2015-10-09 CN CN201520779290.4U patent/CN205119874U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106838956A (en) * | 2017-01-13 | 2017-06-13 | 安徽未名鼎和环保有限公司 | A kind of refuse burner exhaust gas processing device |
| CN107914343A (en) * | 2017-11-30 | 2018-04-17 | 双钱集团（江苏）轮胎有限公司 | A kind of new temperature control device for Banbury mixer |
| CN108592491A (en) * | 2018-04-24 | 2018-09-28 | 河南龙丰实业股份有限公司 | The inorganic refrigerated energy-saving down cycles system of culture medium of edible fungus cooling chamber |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160330 Termination date: 20191009 |