CN202061547U - UV (ultraviolet) photolysis purifying equipment for high-concentration foul waste gas in oilfields - Google Patents
UV (ultraviolet) photolysis purifying equipment for high-concentration foul waste gas in oilfields Download PDFInfo
- Publication number
- CN202061547U CN202061547U CN2011201242940U CN201120124294U CN202061547U CN 202061547 U CN202061547 U CN 202061547U CN 2011201242940 U CN2011201242940 U CN 2011201242940U CN 201120124294 U CN201120124294 U CN 201120124294U CN 202061547 U CN202061547 U CN 202061547U
- Authority
- CN
- China
- Prior art keywords
- waste gas
- gas
- cleaning equipment
- high concentration
- oil field
- 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
Images
Abstract
The utility model discloses UV(ultraviolet) photolysis purifying equipment for high-concentration foul waste gas in oilfields, which comprises a waste gas feed device, a waste gas treatment device and a purified gas discharge device connected in sequence. The waste gas feed device comprises a waste gas delivery pipeline and an air inlet communicated with the external, the waste gas treatment device comprises a reaction chamber and an exhaust fan arranged at the back of the reaction chamber and communicated with the same, the reaction chamber is communicated with the waste gas delivery pipeline, and multiple groups of UV transmitting tubes are arranged in the reaction chamber. The UV photolysis purifying equipment for high-concentration foul waste gas in oilfields is capable of removing foul waste gas produced in natural gas hydration purifying process for foul oil (gas) fields effectively, is low in cost, high in gas treatment capacity and free of secondary pollution.
Description
Technical field
The utility model relates to a kind of cleaning equipment, relates in particular to a kind of oil field high concentration foul waste gas UV photodissociation cleaning equipment.
Background technology
In the gas gathering station in (gas) field that recovers the oil, employing triethylene glycol (TEG) technology removes the moisture in the natural gas, the dewater unit discharge tail gas contains the gas of a certain amount of hydrogen sulfide, methane, NMHC, steam, TEG and other complicated component in the dehydration, and this will diminish the healthy of staff and surrounding enviroment are caused negative effect.
The northern territory that generally distributes, the oil recovery of China (gas) field, and belong to open work mostly, day and night temperature is big, summer in winter maximum temperature difference even up to more than 60 ℃.The exhaust gas constituents complexity that produces in the dehydration, water content height, temperature height; And plant area's requirement of explosion proof is high.In recent years, never find fairly perfect technical scheme to solve this waste gas problem.
The purified treatment means of the high concentration foul waste gas that in the industry purification treatment factory is produced in process of production mainly comprise at present: 1) direct high-temperature combustion method; 2) catalytic oxidation; 3) ozone deodorization process; 4) active carbon adsorption; 5) soda acid soup spray process; 6) biological deodorizing method etc.These methods have equipment investment height, operating cost height in varying degrees, handle narrow-minded, job insecurity, take up room big, the deodorization purification efficiency is not high, have potential safety hazard, have secondary pollution problems.
The utility model content
The technical problems to be solved in the utility model is, at the above-mentioned operating cost height of prior art, processing is narrow-minded, the deodorization purification efficiency is not high and have defective such as secondary pollution, provide a kind of and can efficiently remove the foul waste gas that produces in the gas dehydration process for purifying of oil (gas) field and operating cost is low, treating capacity big and the oil field high concentration foul waste gas UV photodissociation cleaning equipment of non-secondary pollution.
The technical scheme that its technical problem that solves the utility model adopts is: a kind of oil field high concentration foul waste gas UV photodissociation cleaning equipment is provided, comprises in turn gas eduction unit after waste gas gatherer, emission-control equipment and the purification that connects;
Described waste gas gatherer comprises waste gas pipeline road and air inlet, and described air inlet communicates with the external world;
The air exhauster that described emission-control equipment comprises reative cell and is provided with and is communicated with reative cell behind reative cell, described reative cell is communicated with described waste gas pipeline road, and many group UV transmitting tubes are set in the described reative cell.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described oil field high concentration foul waste gas UV photodissociation cleaning equipment also comprises automaton.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described emission-control equipment also comprises and is used for baffle device for water that foul waste gas moisture is held back, before described baffle device for water is arranged on reative cell.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described baffle device for water bottom is provided with condensate draining.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described waste gas pipeline road comprises exhaust pipe and gas sampling pipe, and described gas sampling pipe is communicated with described reative cell; Be provided with the gas sampling cover between described exhaust pipe and the described gas sampling pipe, described exhaust pipe, described gas sampling pipe and gas sampling cover are communicated with.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described air inlet is arranged on the described gas sampling cover and with the external world and communicates.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, condensate drain outlet is set in the bottom of described gas sampling cover.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described purification back gas eduction unit comprises the purified gas delivery pipe, and described purified gas delivery pipe is communicated with described air exhauster.
UV photodissociation cleaning equipment is in high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described automaton comprises electric cabinet, master controller, the Abgassensor and the memory that are connected with described master controller, described master controller and memory are arranged in the described electric cabinet, and described Abgassensor is arranged in the described gas sampling pipe.
In high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, described electric cabinet is that explosion-proof casing and described master controller and memory are respectively explosion-proof master controller and explosion-proof memory.
The utility model, has following beneficial effect: owing on the one hand the foul gas molecule is carried out cracking by the many groups UV transmitting tube that is provided with in the reative cell, on the other hand the oxygen reaction in the reative cell is produced ozone, the foul gas molecule purifies by ozone Oxidation Treatment again, UV cracking and ozone oxidation coordinated, the waste exhaust gases that multiple independent employing cracking or ozone oxidation can't be able to be handled is decomposed comparatively up hill and dale, and purified treatment is effective, efficient is high.Participate in cracking and ozone oxidation reaction owing to need not to add any chemical substance in the entire process process, only need provide necessary electric power to get final product, so operating cost is low; Waste gas material molecular link is after cracking, oxidation deodorizing purified treatment, and no discarded object and sewage produce, so non-secondary pollution; The utility model adopts the form work continuously, and is provided with corresponding exhaust duct and air draft power, can suck pending foul waste gas continuously and discharge purified gas, therefore can work continuously, and handle large-minded and efficient high.In addition, in the waste gas gatherer air inlet is set, air inlet communicates with the external world; When waste gas is inhaled into, also outside air is sucked, increased the oxygen content in the waste gas, make the ozone that in reative cell, can produce q.s be used to handle waste gas.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples, in the accompanying drawing:
Fig. 1 is the structural representation according to the oil field high concentration foul waste gas UV photodissociation cleaning equipment of the utility model embodiment;
Fig. 2 is the stereogram according to emission-control equipment in the oil field high concentration foul waste gas UV photodissociation cleaning equipment of the utility model embodiment;
Fig. 3 is the vertical view according to the internal structure of emission-control equipment in the oil field high concentration foul waste gas UV photodissociation cleaning equipment of the utility model embodiment.
The specific embodiment
Front and back position of the present utility model definition is: according to exhaust gas flow direction, before the orientation that waste gas is introduced into is, after after the orientation that enters is.
In order to make the purpose of this utility model, technical scheme and advantage clearer,, the utility model is further elaborated below in conjunction with drawings and Examples.Should be appreciated that specific embodiment described herein only in order to explanation the utility model, and be not used in qualification the utility model.
As depicted in figs. 1 and 2, gas eduction unit after the oil field of foundation the utility model embodiment high concentration foul waste gas UV photodissociation cleaning equipment comprises waste gas gatherer, emission-control equipment and the purification that connects in turn.Wherein the waste gas gatherer is used to collect pending foul waste gas, and the agent structure of waste gas gatherer is a pipeline configuration, comprises waste gas pipeline road and air inlet 119, and air inlet 119 communicates with the external world, can import outside fresh air.In foundation embodiment of the present utility model, the waste gas pipeline road comprises exhaust pipe 116 and gas sampling pipe 120, between exhaust pipe 116 and the gas sampling pipe 120 gas sampling cover 117 is set, exhaust pipe 116 is communicated with gas sampling pipe 120 by gas sampling cover 117, and gas sampling pipe 120 combines with exhaust gas inlet 111 sealings.In addition, opening can be set to form air inlet 119 on gas sampling pipe 120.Air inlet 119 positions be provided with multiple choices, can select to be arranged on top, bottom or relative exhaust pipe 116 1 sides of gas sampling cover 117, for example in Fig. 2, in the junction of gas sampling cover 117 with exhaust pipe 116, the latter half of gas sampling cover 117 1 sides combines with exhaust pipe 116 sealings, and the first half is provided with opening formation air inlet 119.Also condensate drain outlet 118 can be set in the bottom of gas sampling cover 117, can in time discharge condensed water.
In the present embodiment, as shown in Figure 2, for example emission-control equipment can be arranged in the seal case, this casing floor space is little, is suitable for arranging the narrow and small specific condition of compactness and place; And can preferably exhaust gas inlet 111 be set, and clean gas outlet 112 be set at the top of casing in the left side of this casing.Exhaust gas inlet 111 is communicated with gas sampling pipe 120.As shown in Figure 1, baffle device for water 114 can be set in emission-control equipment preferably, the inlet of this baffle device for water 114 is communicated with exhaust gas inlet 111, the condensation of the elder generation of the moisture in the foul waste gas can be removed.Correspondingly, condensate draining 115 can be set, to be used for the condensed water that the collection and purification process is discharged in the bottom of baffle device for water 114.The bottom of condensate draining 115 is provided with discharge outlet 123, can in time discharge the condensed water in the purification process.
Described emission-control equipment comprises reative cell 110, and reative cell 110 can directly be communicated with the waste gas gatherer; Also the inlet of reative cell 110 can be communicated with the outlet of baffle device for water 114, be communicated with the waste gas gatherer by baffle device for water 114.Shown in Fig. 1,3, reative cell 110 is made by stainless steel material, is provided with many high-power high energy UV transmitting tubes of group and suitable with it multi-group power module groups in it.The position of UV transmitting tube is provided with multiple choices, can also can be parallel to the base plate setting perpendicular to the base plate setting of emission-control equipment casing, not special restriction.Fig. 3 shows a kind of selection that is provided with, and it is parallel with the base plate of casing that the UV transmitting tube is set.
Described emission-control equipment comprises air exhauster 113, to provide air draft power to oil field high concentration foul waste gas UV photodissociation cleaning equipment.Air exhauster 113 is arranged on after the reative cell 110.Air exhauster 113 also is communicated with reative cell 110 and purification back gas eduction unit respectively simultaneously.
Comprise purified gas delivery pipe 121 according to gas eduction unit after the purification of the utility model embodiment, Purge gas delivery pipe 121 is tightly connected with purified gas floss hole 112, thereby is communicated with described air exhauster 113.Simultaneously load-bearing fixture 122 is set, to fix Purge gas delivery pipe 121, for example is fixed on the wall or on the support, to guarantee to derive smoothly purified gas around Purge gas delivery pipe 121.
In an embodiment of the present utility model, be provided with automaton in the oil field high concentration foul waste gas UV photodissociation cleaning equipment, automaton can not be provided with yet.Automaton comprises electric cabinet, master controller, the Abgassensor that is connected with master controller and memory, master controller and memory are arranged in the electric cabinet, Abgassensor is arranged in the gas sampling pipe 120, and master controller also is connected with the factory supervisory control desk with the power module group respectively.For security of operation, electric cabinet is that explosion-proof casing and master controller and memory are respectively explosion-proof master controller and explosion-proof memory, and the electronic devices and components in the electric cabinet adopt explosion-proof electronic devices and components.And the negative-pressure air-flow thermovent is set in the control room, when ensureing the normal operation of electric components, guarantee that high concentration foul waste gas UV photodissociation cleaning equipment in oil field does not constitute potential safety hazard to the safety in oil (gas) field.
Shown in arrow among Fig. 2, pending foul waste gas enters gas sampling cover 117 rapidly after feeding exhaust pipe 116 under the effect of air exhauster 113.Meanwhile, be provided with air inlet 119 on gas sampling cover 117, this air inlet 119 communicates with the external world.Under the effect of air exhauster 113, outside fresh air enters into gas sampling cover 117 by this air inlet 119 continuously, and the fresh air that is sucked continues to enter emission-control equipment at the effect lower edge of air exhauster 113 gas sampling pipe 120 with the foul waste gas that feeds from exhaust pipe 116.In this course of conveying, because fresh air and foul waste gas are together carried, fresh air can play the good cooling effect to foul waste gas.And the condensate drain outlet 118 that gas sampling cover 117 bottoms are provided with can be discharged condensed water in time.
Under the effect of air exhauster 113, foul waste gas and fresh air enter exhaust gas inlet 111 from gas sampling pipe 120 together.As shown in Figure 1, if exhaust gas inlet 111 back are provided with baffle device for water 114, then pending foul waste gas is discharged after a large amount of water recoveries of carrying wherein through after the processing of baffle device for water 114.The condensed water that the condensate draining 115 that baffle device for water 114 bottoms are provided with discharges in can the collection and purification process.Condensate draining 115 bottoms are provided with non-discharge outlet 123 can in time discharge the condensed water that condensate draining 115 is collected.
Table 1: molecular link in the foul waste gas and corresponding binding energy
| In conjunction with | Binding energy (KJ/mol) | In conjunction with | Binding energy (KJ/mol) |
| H-H | 436.2 | C-H | 413.6 |
| H-C | 347.9 | C-F | 441.2 |
| C-C | 607.0 | C-N | 291.2 |
| C＝C | 828.8 | C＝N | 791.2 |
| N-N | 160.7 | C-O | 351.6 |
| O-O | 139.0 | C＝O | 724.2 |
| O＝O | 490.6 | O-H | 463.0 |
Emission-control equipment comprises reative cell 110, and the inlet of reative cell 110 can directly be communicated with exhaust gas inlet 111, also can preferably be communicated with the outlet of baffle device for water 114.Shown in Fig. 1,3, reative cell 110 is made by stainless steel material, is provided with many high-power high energy UV transmitting tubes of group and suitable with it multi-group power module groups in it.The UV transmitting tube preferably adopts high-power high energy UV transmitting tube, belongs to the low-pressure mercury discharge tube, and the wavelengths of ultraviolet radiation of sending is 160nm～200nm, and corresponding photon energy is respectively 800KJ/mol and 472KJ/mol.And if want the molecular link of cracking foul waste gas molecule, the photon energy of being launched must be higher than the binding energy of foul waste gas molecular link.In the utility model, pending foul waste gas mainly comprises the gas of hydrogen sulfide, methane, NMHC, steam, TEG and other complicated component, and table 1 has been listed main molecules key and the pairing binding energy of this molecule that comprises in the foul waste gas.As can be seen from Table 1, except the C=C key, the photon energy of UV ray is higher than the binding energy of other molecular link in the table 1, and the molecule binding energy of general most of chemical substances is lower than the photon energy of 160nm and 200nm wavelength high energy ultraviolet rays, so this oil field high concentration foul waste gas UV photodissociation cleaning equipment can the most of chemical substances molecular link of cracking except carbon and metal.Under high energy UV radiation exposure, the molecule cracking in the foul waste gas is converted into atom and the radical ion that is ionic condition.Therefore after foul waste gas enters the reative cell 110 that is provided with many group high energy UV transmitting tubes, can finish cracking reaction therein.
On the other hand, under the effect of air exhauster 113, air inlet 119 can absorb fresh air continuously and enter from the external world, these fresh airs can not only be lowered the temperature to foul waste gas in course of conveying, and abundant oxygen is provided can also for reative cell 110, after entering into reative cell 110, under the direct irradiation of many group high energy UV transmitting tubes, oxygen molecule cracking in the fresh air generates ozone, and its chemical process is as follows:
UV (160nm-200nm)+O
2→ O
-+ O
+(active oxygen); O
*+ O
2→ O
3(ozone).
The active ozone of the character that is generated will be cracked into the atom that is ionic condition and the foul waste gas of radical ion and carry out strong oxidation reaction, these foul gas through UV irradiation cracking are reassembled into the compound of harmless or low evil, as water, carbon dioxide etc., no discarded object and sewage produce in this oxidizing process, therefore can not produce secondary pollution to environment.Table 2 has been listed the molecular weight of part foul waste gas material, and has listed cracking, the oxidizing process of material molecule key in the foul waste gas:
UV(160nm-200nm)→H
2S＝H
++H
-+S→H+O
3S+O
3→H
2O SO
2
UV(160nm-200nm)→COS＝C+O+S→C+O
3O+O
3S+O
3→CO
2SO
2
UV(160nm-200nm)→CS
2＝C+O
3S
-+S
++O
3→CO
2SO
2。
Table 2: the molecular weight of part foul waste gas material
| Title | Molecular weight | Title | Molecular weight |
| Hydrogen sulfide | 34.08 | Methyl mercaptan | 48.13 |
| Methyl sulfide | 62.13 | Dimethyl disulfide | 94.20 |
| Toluene | 92.14 | Methylamine | 31.06 |
| Ethylenediamine | 60.10 | Ethanol | 46.07 |
From as can be seen above, the reaction in the reative cell 110 comprises two aspects: be foul waste gas cracking under the direct irradiation of high energy UV ray on the one hand, form the atom and the radical ion that are ionic condition; Be that the fresh air that the high energy UV radiation exposure external world enters generates the active ozone of character on the other hand, the foul waste gas after ozone and the cracking carries out the compound that strong oxidation reaction generates harmless or low evil.Therefore, by above-mentioned cracking and oxidation reaction, can efficiently remove the gas dehydration purifying exhaust air: the gas of hydrogen sulfide, methane, NMHC, steam, TEG solution and other complicated components, deodorising effect surpasses the odorant pollutant discharge standard limit value (GB14554-93) of country's promulgation in 1993.In addition, be direct photodissociation and ozone oxidation in the purification process, and ozone form by the illumination fresh air, therefore need not to add other chemical substance, only electric power need be provided and corresponding exhaust duct be set and air draft power.Air draft power and baffle device for water are set simultaneously, make oil field high concentration foul waste gas UV photodissociation cleaning equipment can purify the foul waste gas of high concentration, atm number, the big temperature difference and big water content effectively, adaptability is strong, but every days 24 continuous throughout the twenty-four hour24, stable and reliable operation.Except conveyance conduit, the main part of oil field high concentration foul waste gas UV photodissociation cleaning equipment has only air exhauster and reative cell, and only be provided with to organize UV transmitting tubes and adaptive with it power module groups in the reative cell more, therefore the cleaning equipment floor space is little, from heavy and light, be suitable for arranging specific conditions such as compact, that the place is narrow and small.And simple installation and operating cost are low, there is not any mechanical action, noiselessness, need not personal management and regular maintenance, only need to make regular check on, the cleaning equipment energy consumption is low, (every processing waste gas air quantity is 1000 cubic metres/hour, about 0.2 degree of power consumption only), UV cleaning equipment windage is extremely low＜50pa, can save a large amount of air draft power consumptions.Waste gas purification carries out processed before handling simultaneously, and is provided with drainage arrangement.Need not to carry out other particular processing, as acid/neutralizing treatment, dedusting etc.Equipment is between-30 ℃～95 ℃ Celsius, and pH value is between 3～11, but humidity is in equal operate as normal below 98%.Cleaning equipment adopts the manufacturing of high-quality anti-corrosion material, fire prevention, explosion-proof, decay resistance is high, long service life.
In an embodiment of the present utility model, be provided with automaton in the oil field high concentration foul waste gas UV photodissociation cleaning equipment, automaton comprises master controller and the Abgassensor and the memory that are connected with above-mentioned master controller, Abgassensor is positioned at gas sampling pipe 120, and master controller also is connected with the factory supervisory control desk with the power module group respectively.Automatically control utilizes Abgassensor to measure data such as exhaust gas concentration, temperature, humidity, tolerance, and automaton can be adjusted cleaning equipment high energy UV ray power output and ozone generating amount automatically, thereby reaches the best purification effect.Also can store, equipment fault or abnormal accident are given the alarm etc., also can be connected to carry out online monitoring with factory's master control platform to the service data of oil field high concentration foul waste gas UV photodissociation cleaning equipment.For security of operation, automaton comprises explosion-proof components and parts and explosion-proof casing.And the negative-pressure air-flow thermovent is set in the control room, when ensureing the normal operation of electric components, guarantee that high concentration foul waste gas UV photodissociation cleaning equipment in oil field does not constitute potential safety hazard to the safety in oil (gas) field.
Adopt according to high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model, can efficiently remove the gas dehydration purifying exhaust air: the gas of hydrogen sulfide, methane, NMHC, steam, TEG solution and other complicated components, deodorising effect surpass the odorant pollutant discharging primary standard (GB14554-93) of country's promulgation in 1993.The key technical indexes according to high concentration foul waste gas UV photodissociation cleaning equipment in oil field of the present utility model is as follows:
1, in the reative cell inside of cleaning equipment, apart from high energy UV ray emission pipe 10cm place, the amount intensity of UV ray is: 6000 μ w/cm
2
2, under UV cleaning equipment Light Condition, the start operation is after 10 minutes, and in reative cell, ozone concentration reaches 800mg/m
3More than.
3, this UV cleaning equipment, practical application through tens remainder engineerings, sewage treatment plant, sewage pump station, destructor plant, pharmaceutical factory, chemical plant or the like waste gas is carried out deodorization purify, the deodorization purifying rate of foul waste gas such as hydrogen sulfide, ammonia, VOC is reached more than 99%.
Should be understood that, for those of ordinary skills, can be improved according to the above description or conversion, and all these improvement and conversion all should belong to the protection domain of the utility model claims.
Claims (10)
1. an oil field high concentration foul waste gas UV photodissociation cleaning equipment is characterized in that, comprises in turn gas eduction unit after waste gas gatherer, emission-control equipment and the purification that connects;
Described waste gas gatherer comprises waste gas pipeline road and air inlet (119), and described air inlet (119) communicates with the external world;
Described emission-control equipment comprises reative cell (110) and the air exhauster (113) that is provided with and is communicated with reative cell (110) in reative cell (110) back, described reative cell (110) is communicated with described waste gas pipeline road, and many group UV transmitting tubes are set in the described reative cell (110).
2. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 1 is characterized in that, described oil field high concentration foul waste gas UV photodissociation cleaning equipment also comprises automaton.
3. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 1 and 2, it is characterized in that, described emission-control equipment comprises also and is used for baffle device for water (114) that foul waste gas moisture is held back that it is preceding that described baffle device for water is arranged on reative cell (110).
4. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 3 is characterized in that, described baffle device for water bottom (114) is provided with condensate draining (115).
5. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 1 and 2, it is characterized in that, described waste gas pipeline road comprises exhaust pipe (116) and gas sampling pipe (120), and described gas sampling pipe (120) is communicated with described reative cell (110); Be provided with gas sampling cover (117) between described exhaust pipe (116) and the described gas sampling pipe (120), described exhaust pipe (116), described gas sampling pipe and gas sampling cover (117) are communicated with.
6. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 5 is characterized in that, described air inlet (119) is arranged on described gas sampling cover (117) and upward and with the external world communicates.
7. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 6 is characterized in that, in the bottom of described gas sampling cover (117) condensate drain outlet (118) is set.
8. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 1 and 2, it is characterized in that, described purification back gas eduction unit comprises purified gas delivery pipe (121), and described purified gas delivery pipe (121) is communicated with described air exhauster (113).
9. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 2, it is characterized in that, described automaton comprises electric cabinet, master controller, the Abgassensor and the memory that are connected with described master controller, described master controller and memory are arranged in the described electric cabinet, and described Abgassensor is arranged in the described gas sampling pipe (120).
10. high concentration foul waste gas UV photodissociation cleaning equipment in oil field according to claim 9 is characterized in that, described electric cabinet is that explosion-proof casing and described master controller and memory are respectively explosion-proof master controller and explosion-proof memory.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201242940U CN202061547U (en) | 2011-04-25 | 2011-04-25 | UV (ultraviolet) photolysis purifying equipment for high-concentration foul waste gas in oilfields |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011201242940U CN202061547U (en) | 2011-04-25 | 2011-04-25 | UV (ultraviolet) photolysis purifying equipment for high-concentration foul waste gas in oilfields |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202061547U true CN202061547U (en) | 2011-12-07 |
Family
ID=45055429
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011201242940U Expired - Fee Related CN202061547U (en) | 2011-04-25 | 2011-04-25 | UV (ultraviolet) photolysis purifying equipment for high-concentration foul waste gas in oilfields |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202061547U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104785051A (en) * | 2014-01-21 | 2015-07-22 | 吴江新生针纺织有限责任公司 | Heat recovery and oil-gas separation combination device |
| CN106823732A (en) * | 2017-02-21 | 2017-06-13 | 安徽海纳森环境科技有限公司 | A kind of high efficiency smart photodissociation cleaning equipment |
| CN108554036A (en) * | 2018-03-15 | 2018-09-21 | 盐城市虹艳化工有限公司 | A kind of chemical workshop emission-control equipment |
-
2011
- 2011-04-25 CN CN2011201242940U patent/CN202061547U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104785051A (en) * | 2014-01-21 | 2015-07-22 | 吴江新生针纺织有限责任公司 | Heat recovery and oil-gas separation combination device |
| CN106823732A (en) * | 2017-02-21 | 2017-06-13 | 安徽海纳森环境科技有限公司 | A kind of high efficiency smart photodissociation cleaning equipment |
| CN108554036A (en) * | 2018-03-15 | 2018-09-21 | 盐城市虹艳化工有限公司 | A kind of chemical workshop emission-control equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN204247050U (en) | A kind of sludge drying produces foul gas UV photodissociation cleaning equipment | |
| CN207153435U (en) | Container-type difficult degradation organic exhaust gas plasma and life assemblage method processing unit | |
| CN202061547U (en) | UV (ultraviolet) photolysis purifying equipment for high-concentration foul waste gas in oilfields | |
| CN201632187U (en) | Purification treatment equipment for high-concentration obnoxious gas and industrial waste gas | |
| CN204107266U (en) | A kind of Car Spraying-Paint Room waste gas UV photodissociation cleaning equipment | |
| CN204337990U (en) | A kind of UV photodissociation cleaning equipment processing petrifaction sewage stench | |
| WO2011047507A1 (en) | Method and equipment for purifying high concentration malodorous gas and industrial waste gas | |
| CN105157048A (en) | Boiler waste gas utilization device | |
| CN207270995U (en) | A kind of adsoption catalysis integration waste gas pollution control and treatment equipment | |
| CN205164470U (en) | Exhaust purifying device | |
| CN206444425U (en) | UV photodissociation clarifiers | |
| CN204233959U (en) | Petrochemical industry storage tank high-concentration organic waste gas UV photodissociation cleaning equipment | |
| CN205627631U (en) | Foul gas photodissociation catalytic oxidation equipment | |
| CN203108425U (en) | Hydrogen sulfide waste gas purification equipment | |
| CN205627572U (en) | Landfill leachate foul gas purifies integrated equipment | |
| CN205868003U (en) | Combination formula processing apparatus of industrial fumes waste gas | |
| CN206121518U (en) | Novel waste gas treating system | |
| CN211586008U (en) | Flue gas purification device for desulfurization and denitrification | |
| CN211273953U (en) | Sewage treatment system | |
| CN204236319U (en) | Portable foul gas UV photodissociation clean-up device | |
| CN203469781U (en) | UV light oxygen deodorizer | |
| WO2017035923A1 (en) | Biomass gasification-based power generation system | |
| CN218221851U (en) | Ternary purification module for gas deodorization | |
| CN111265991A (en) | Flue gas deacidification purification device for waste incineration power generation | |
| CN204073764U (en) | Photodissociation cooking fume remover |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C56 | Change in the name or address of the patentee | ||
| CP03 | Change of name, title or address |
Address after: 518000, C, building, building A, Pu Hua Science Park, big wave Street Industrial Road, Longhua New District, Guangdong, China Patentee after: SHENZHEN THY ENVIRONMENTAL PROTECTION INC. Address before: 518034 deep Mao business center, 59 news Road, Guangdong, Shenzhen, 610-613, Futian District Patentee before: Shenzhen Tianhaoyang Environmental Technology Co., Ltd. |
|
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20111207 Termination date: 20200425 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |