CN203935758U - A kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption - Google Patents
A kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption Download PDFInfo
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- CN203935758U CN203935758U CN201420385539.9U CN201420385539U CN203935758U CN 203935758 U CN203935758 U CN 203935758U CN 201420385539 U CN201420385539 U CN 201420385539U CN 203935758 U CN203935758 U CN 203935758U
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- Prior art keywords
- oil
- absorption tower
- absorption
- gas
- adsorption
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- 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 - Lifetime
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- 238000010521 absorption reaction Methods 0.000 title claims abstract description 75
- 238000011084 recovery Methods 0.000 title claims abstract description 25
- 238000001179 sorption measurement Methods 0.000 title claims abstract description 17
- 239000002250 absorbent Substances 0.000 claims abstract description 30
- 230000002745 absorbent Effects 0.000 claims abstract description 30
- 239000003610 charcoal Substances 0.000 claims abstract description 25
- 230000000740 bleeding effect Effects 0.000 claims description 9
- 238000005057 refrigeration Methods 0.000 claims description 9
- 230000008676 import Effects 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 22
- 229930195733 hydrocarbon Natural products 0.000 abstract description 13
- 150000002430 hydrocarbons Chemical class 0.000 abstract description 13
- 239000004215 Carbon black (E152) Substances 0.000 abstract description 9
- 229910052799 carbon Inorganic materials 0.000 abstract description 6
- 229920006395 saturated elastomer Polymers 0.000 abstract description 4
- 238000003795 desorption Methods 0.000 abstract description 3
- 230000009885 systemic effect Effects 0.000 abstract description 2
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 9
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 9
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical group OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000008096 xylene Substances 0.000 description 3
- 239000003463 adsorbent Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 108010004350 tyrosine-rich amelogenin polypeptide Proteins 0.000 description 1
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
The utility model relates to a kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption, this device for recovering oil and gas comprises to be sent into untreated oil gas in absorption tower by conveying fan and appendix, in absorption tower, by absorbent, absorb the hydrocarbon in untreated oil gas, the Volatile Gas of absorbent and unabsorbed oil gas are discharged from absorbing tower top, by the intake valve of opening, enter charcoal trap, charcoal trap absorbs saturated rear intake valve and closes bleed valve unlatching, high concentration desorb oil gas after being adsorbed enters in absorption tower by vavuum pump, a side on absorption tower is provided with oil-out by flowline and scavenge oil pump, the systemic absorbent in absorption tower and oil plant are sent in oil storage tank, one side on absorption tower is provided with heat exchanger and the cooling-cycle apparatus of absorbent.This device can effectively reclaim the various hydrocarbons in oil gas, and absorptivity is brought up to more than 99%, can greatly alleviate and be difficult for the impact of the gas of desorption desorb on active carbon, thereby realize effective recovery of hydrocarbon.
Description
Technical field
The utility model relates to organic exhaust gas recovery and utilization technology, is specifically related to a kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption.
Background technology
Effective recovery technology of the domestic and international hydrocarbon for oil gas, is mainly used charcoal absorption to add absorption plant at present, condensing unit, and film adds absorption plant.
Charcoal absorption absorption plant need to use absorbent, and the advantage of charcoal absorption absorption plant makes the stability of a system high, safe, and energy consumption is low.But absorption organic gas composition is had to certain limitation, and the organic gas that is difficult for desorb is not suitable for the method.Therefore be necessary the recovery technology of existing hydrocarbon to improve.
Utility model content
The purpose of this utility model is, overcome defect of the prior art, a kind of various hydrocarbons that can effectively reclaim in oil gas are provided, as long as select the absorbent of the easy desorb of rational active carbon, utilize cold absorbent to coming gas to absorb, absorptivity is brought up to more than 99%, can greatly be alleviated and be difficult for the impact of the gas of desorption desorb on active carbon, thereby realize effective recovery of hydrocarbon.
The technical scheme that the utility model is dealt with problems is: a kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption is provided, it is characterized in that, this device for recovering oil and gas comprises the appendix being connected with conveying fan, appendix is connected with absorption tower, in absorption tower, be provided with absorbent, the top on absorption tower is provided with blast pipe, blast pipe is connected with charcoal trap by intake valve, the portion that charcoal trap is inhaled is provided with bleed valve, bleed valve is connected with absorption tower by vavuum pump again, a side on absorption tower is provided with oil-out, oil-out is connected with oil storage tank by flowline and scavenge oil pump, a side on absorption tower is provided with heat exchanger and the cooling-cycle apparatus of absorbent.
Wherein preferred technical scheme is that described heat exchanger is for being reduced to the temperature of absorption tower inner absorbent below 10 degree.
Preferred technical scheme also has, and described charcoal trap is at least provided with two and be connected in parallel, and each charcoal trap is respectively equipped with intake valve and bleed valve, and the intake valve on each charcoal trap and bleed valve are alternately opened or close.
Further preferred technical scheme also has, and described in each, the upper end of charcoal trap is respectively equipped with tail gas air bleeding valve, the unlatching of tail gas air bleeding valve or close with the unlatching of bleed valve or close and synchronize.
Preferred technical scheme also has, described cooling-cycle apparatus includes circulating pump, heat exchanger and refrigeration unit, the import of circulating pump is connected with absorption tower by pipeline, circulation delivery side of pump is connected with the inlet of heat exchanger by pipeline, the liquid outlet of heat exchanger is connected with absorption tower by the road, in a side of heat exchanger, is connected with refrigeration unit.
Preferred technical scheme also has, and between described oil storage tank and absorption tower, is connected with and loops back oil pipe line, is provided with the second circulating pump on return line.
Preferred technical scheme also has, and described untreated oil gas at least includes benzene,toluene,xylene, and described adsorbent is ethylene glycol.
Preferred technical scheme also has, and described intake valve, bleed valve and tail gas air bleeding valve are magnetic valve.
Compared with prior art, the beneficial effects of the utility model are: this cold oil pre-absorption Vapor Recovery Equipment with Adsorption, by refrigerant compression mechanism cold, heat exchanger heat exchange, absorbent in absorption tower is cooled to below 10 ℃, greatly strengthen absorbent to carrying out aspiration adduction, because adopt absorption tower inner absorbent refrigeration partial circulating, energy consumption reduces greatly simultaneously.For there being the absorbing in absorbent of the organic principle that is difficult for desorb 99% wherein, alleviated the replacement cycle of active carbon, also reduced the number of times of desorb.This cold oil pre-absorption Vapor Recovery Equipment with Adsorption can also effectively reclaim the various hydrocarbons in oil gas, as long as select the absorbent of the easy desorb of rational active carbon, utilize cold absorbent to coming gas to absorb, absorptivity can reach more than 99%, greatly alleviated and be difficult for the impact of the gas of desorption desorb on active carbon, thereby realized effective recovery of hydrocarbon.This cold oil pre-absorption Vapor Recovery Equipment with Adsorption can also reclaim the hydrocarbons such as benzene,toluene,xylene to become valuable product, makes concentration of oil and gas discharged <25g/m
3, efficiency of oil & gas processing reaches 95%, and the recovery of triphen simultaneously reaches more than 99%, and discharge reaches the requirement of discharge standard of air pollutants.
Accompanying drawing explanation
Fig. 1 is the utility model cold oil pre-absorption Vapor Recovery Equipment with Adsorption block diagram.
In figure: 1-conveying fan, 2-appendix, 3-absorption tower, 4-charcoal trap, 5-intake valve, 6-bleed valve, 7-vavuum pump, 8-oil-out, 9-flowline, 10-scavenge oil pump, 11-oil storage tank, 12-heat exchanger, 13-tail gas air bleeding valve, 14-circulating pump, 15-refrigeration unit, 16-loops back oil pipe line, 17-the second circulating pump.
The specific embodiment
The utility model is a kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption, this device for recovering oil and gas comprises to be sent into untreated oil gas in absorption tower 3 by conveying fan 1 and appendix 2, in absorption tower 3, by absorbent, absorb the hydrocarbon in untreated oil gas, the Volatile Gas of absorbent and unabsorbed oil gas are discharged on 3 tops from absorption tower, by the intake valve 5 of opening, enter charcoal trap 4, charcoal trap 4 absorbs saturated rear intake valve 5 and closes bleed valve 6 unlatchings, by the high concentration desorb oil gas after charcoal trap 4 absorption, by vavuum pump 7, again entered in absorption tower 3, on absorption tower, a side of 3 is provided with oil-out 8, oil-out 8 is by flowline 9 and scavenge oil pump 10, the systemic absorbent in absorption tower 3 and oil plant are sent in oil storage tank 11, on absorption tower, a side of 3 is provided with heat exchanger 12 and the cooling-cycle apparatus of absorbent.
In the utility model, preferred embodiment is that described heat exchanger is for being reduced to the temperature of absorption tower inner absorbent below 10 degree.
In the utility model, preferred embodiment also has, described charcoal trap 4 is at least provided with two and be connected in parallel, each charcoal trap 4 is respectively equipped with intake valve 5 and bleed valve 6, and the intake valve on each charcoal trap 45 alternately opens or cuts out with bleed valve 6.
In the utility model, further preferred embodiment also has, and described in each, the upper end of charcoal trap 4 is respectively equipped with tail gas air bleeding valve 13, the unlatching of tail gas air bleeding valve 13 or close with the unlatching of bleed valve 6 or close and synchronize.
In the utility model, preferred embodiment also has, described cooling-cycle apparatus includes circulating pump 14, heat exchanger 12 and refrigeration unit 15, the import of circulating pump 14 is connected with absorption tower 3 by pipeline, the outlet of circulating pump 14 is connected with the inlet of heat exchanger 12 by pipeline, the liquid outlet of heat exchanger 12 is connected with absorption tower 3 by the road, in a side of heat exchanger 12, is connected with refrigeration unit 15.
In the utility model, preferred embodiment also has, and between described oil storage tank 11 and absorption tower 3, is connected with and loops back oil pipe line 16, is provided with the second circulating pump 17 on return line.
In the utility model, preferred embodiment also has, and described untreated oil gas at least includes benzene,toluene,xylene, and described adsorbent is ethylene glycol.
In the utility model, preferred embodiment also has, and described intake valve 5, bleed valve 6 and tail gas air bleeding valve 13 are magnetic valve.
The process that reclaims hydrocarbon gas by this cold oil pre-absorption Vapor Recovery Equipment with Adsorption comprises:
1, oil gas is sent into the absorption tower 3 of gas recovery system for oil through gas path pipe, and absorption tower 3 absorbs own hydrocarbon wherein by absorbent.The Volatile Gas of absorbent and unabsorbed oil gas are discharged from tower top.
2, absorb tower top discharge gas and enter activated carbon adsorber 4, switch to the second activated carbon adsorber 4 and adsorb after the first activated carbon adsorber 4 absorption are saturated, the first activated carbon adsorber 4 carries out oil gas desorb; After the second activated carbon adsorber 4 absorption are saturated, switch to the first activated carbon adsorber 4, the second activated carbon adsorbers 4 and carry out desorb.Two activated carbon adsorber alternations, switching cycle 15-20 minute.
The high concentration stripping gas of 3, discharging from vavuum pump 7 enters absorption tower 3 and absorbs, and the oil gas of the overwhelming majority is absorbed agent and absorbs, and remaining gas is discharged from absorbing tower top, enters circulation.
4, be to guarantee that the temperature of absorption tower 3 inner absorbents is lower than 10 ℃, by circulating pump 14 process heat exchangers 12,15 pairs of absorbents of refrigeration unit, carry out circulating cooling, because be absorption tower inner loop, so energy consumption is lower.
5, the absorbent in absorption tower 3 absorbs oil gas and arrives after a certain amount of, by scavenge oil pump 10, the interior too much absorbent in absorption tower 3 and oil plant are entered to oil storage tank 11; Simultaneously can be according to the uptake of triphen, the absorbent in integral replacing absorption tower at the appropriate time.
The utility model is not limited to above-mentioned embodiment, those skilled in the art make to any apparent improvement of above-mentioned embodiment or change, can not exceed the protection domain of design of the present utility model and claims.
Claims (6)
1. a cold oil pre-absorption Vapor Recovery Equipment with Adsorption, it is characterized in that, this device for recovering oil and gas comprises the appendix being connected with conveying fan, appendix is connected with absorption tower, in absorption tower, be provided with absorbent, the top on absorption tower is provided with blast pipe, blast pipe is connected with charcoal trap by intake valve, the portion that charcoal trap is inhaled is provided with bleed valve, bleed valve is connected with absorption tower by vavuum pump again, a side on absorption tower is provided with oil-out, oil-out is connected with oil storage tank by flowline and scavenge oil pump, a side on absorption tower is provided with heat exchanger and the cooling-cycle apparatus of absorbent.
2. cold oil pre-absorption Vapor Recovery Equipment with Adsorption as claimed in claim 1, it is characterized in that, described charcoal trap is at least provided with two and be connected in parallel, each charcoal trap is respectively equipped with intake valve and bleed valve, and the intake valve on each charcoal trap and bleed valve are alternately opened or close.
3. cold oil pre-absorption Vapor Recovery Equipment with Adsorption as claimed in claim 2, is characterized in that, described in each, the upper end of charcoal trap is respectively equipped with tail gas air bleeding valve.
4. cold oil pre-absorption Vapor Recovery Equipment with Adsorption as claimed in claim 1, it is characterized in that, described cooling-cycle apparatus includes circulating pump, heat exchanger and refrigeration unit, the import of circulating pump is connected with absorption tower by pipeline, circulation delivery side of pump is connected with the inlet of heat exchanger by pipeline, the liquid outlet of heat exchanger is connected with absorption tower by the road, in a side of heat exchanger, is connected with refrigeration unit.
5. cold oil pre-absorption Vapor Recovery Equipment with Adsorption as claimed in claim 1, is characterized in that, between described oil storage tank and absorption tower, is connected with and loops back oil pipe line, is provided with the second circulating pump on return line.
6. cold oil pre-absorption Vapor Recovery Equipment with Adsorption as claimed in claim 2 or claim 3, is characterized in that, described intake valve, bleed valve and tail gas air bleeding valve are magnetic valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420385539.9U CN203935758U (en) | 2014-07-11 | 2014-07-11 | A kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420385539.9U CN203935758U (en) | 2014-07-11 | 2014-07-11 | A kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption |
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| Publication Number | Publication Date |
|---|---|
| CN203935758U true CN203935758U (en) | 2014-11-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420385539.9U Expired - Lifetime CN203935758U (en) | 2014-07-11 | 2014-07-11 | A kind of cold oil pre-absorption Vapor Recovery Equipment with Adsorption |
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| Country | Link |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105861026A (en) * | 2016-05-16 | 2016-08-17 | 湖北楚天蓝环保设备工程有限公司 | Residual oily gas recycling and treatment device and treatment method |
| CN105879570A (en) * | 2016-06-15 | 2016-08-24 | 海湾环境科技（北京）股份有限公司 | Oil gas recycling device and method |
| CN105944498A (en) * | 2016-06-15 | 2016-09-21 | 海湾环境科技（北京）股份有限公司 | Oil vapor recovery system and oil vapor recovery method |
| CN107054922A (en) * | 2017-03-31 | 2017-08-18 | 海湾环境科技（北京）股份有限公司 | Gas recovery system for oil |
| CN112999819A (en) * | 2019-12-20 | 2021-06-22 | 陕西青朗万城环保科技有限公司 | Cold liquid absorption device and system |
-
2014
- 2014-07-11 CN CN201420385539.9U patent/CN203935758U/en not_active Expired - Lifetime
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105861026A (en) * | 2016-05-16 | 2016-08-17 | 湖北楚天蓝环保设备工程有限公司 | Residual oily gas recycling and treatment device and treatment method |
| CN105861026B (en) * | 2016-05-16 | 2018-05-29 | 湖北楚天蓝环保设备工程有限公司 | A kind of slag oil-gas recovery processing device and processing method |
| CN105879570A (en) * | 2016-06-15 | 2016-08-24 | 海湾环境科技（北京）股份有限公司 | Oil gas recycling device and method |
| CN105944498A (en) * | 2016-06-15 | 2016-09-21 | 海湾环境科技（北京）股份有限公司 | Oil vapor recovery system and oil vapor recovery method |
| CN107054922A (en) * | 2017-03-31 | 2017-08-18 | 海湾环境科技（北京）股份有限公司 | Gas recovery system for oil |
| CN112999819A (en) * | 2019-12-20 | 2021-06-22 | 陕西青朗万城环保科技有限公司 | Cold liquid absorption device and system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141112 |