CN201753173U - Apparatus for treating hydrogen sulfide - Google Patents
Apparatus for treating hydrogen sulfide Download PDFInfo
- Publication number
- CN201753173U CN201753173U CN2010202921056U CN201020292105U CN201753173U CN 201753173 U CN201753173 U CN 201753173U CN 2010202921056 U CN2010202921056 U CN 2010202921056U CN 201020292105 U CN201020292105 U CN 201020292105U CN 201753173 U CN201753173 U CN 201753173U
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- process chamber
- chamber
- retort
- pipeline
- adsorber
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- Expired - Fee Related
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Abstract
Provided is an apparatus for treating hydrogen sulfide comprising an oil tank, an air-water two-phase separator, a first reaction pot, a second reaction pot, a three-level absorption reactor and a pipeline, wherein the top of the oil tank is in order serial connection by the pipeline to the air-water two-phase separator, the first reaction pot, the second reaction pot, and then is connected to the three-level absorption reactor. The utility model has plural advantages over prior art technology, such as low manufacturing cost of treatment medium, long running period, safe and convenient operation, changing at any time upon saturation of treat agent, long service lifetime, and no influence on human body or environment due to the dry medium adopted by the utility model.
Description
One, technical field
The utility model relates to the oil and gas industry technical field, a kind of specifically hydrogen sulphide controlling device
Two, background technology
Along with continually developing of oil field, the oil well produced liquid and the accompanying gas of many blocks contain hydrogen sulphide, and serious threat is to personnel's safety.At present, most of units retrain or are equipped with protective device etc. from the personnel operation aspect, can not realize essential safety.Also the chemical neutralisation taked of some unit removes hydrogen sulphide, owing to will contact a large amount of alkaline corrosion media, dangerous, medicament and resultant thereof have than gross pollution soil simultaneously, and the employee adds and to change the labour intensity of reactant liquor bigger simultaneously.
Three, utility model content
The purpose of this utility model is exactly the defective that exists at prior art, and a kind of hydrogen sulphide controlling device is provided.
Its technical scheme is: comprise petrol storage tank, air water two phase separator, first retort, second retort, three grades of absorption reactor thermallies and pipeline.Described petrol storage tank top is connected with three grades of absorption reactor thermallies after pipeline is connected in series air water two phase separator, first retort, second retort successively; Described three grades of absorption reactor thermallies are by three mutual leak free adsorber chambeies, first process chamber and second process chamber connect composition, described adsorber chamber, first process chamber and equal cylinder-like structure of second process chamber or rectangular box structure, its bottom, chamber is equipped with the coil pipe of tail end shutoff, this coil pipe is provided with air extractor vent, the front end of adsorber chamber inner coil pipe extends to outside the chamber, the front end of the first process chamber inner coil pipe is communicated with adsorber top of chamber pipeline, the front end of the second process chamber inner coil pipe is communicated with the first process chamber top duct, the second process chamber top is connected described adsorber chamber with the detection pipeline, also be placed with the processing medicament in first process chamber and second process chamber.
Wherein, the petrol storage tank top duct is provided with compression indicator.The bottom of described air water two phase separator, first retort and second retort is equipped with blow-down pipe.
The utility model has the following advantages compared with prior art:
(1) the treatment media productive costs selected for use of this technology is low, and cycle of run is long, simultaneously workman's easy-to-operate;
(2) inorganic agent is saturated can change later at any time, satisfies the requirement of long-term operation;
(the main medium of 3 these devices is the dryness medium, to human body and not influence of environment.
Four, description of drawings
Fig. 1 is the structural representation of a kind of embodiment of the utility model;
Fig. 2 is the structural representation of three grades of absorption reactor thermallies among Fig. 1.
Five, the specific embodiment
With reference to Fig. 1-Fig. 2, a kind of hydrogen sulphide controlling device comprises petrol storage tank 1, air water two phase separator 3, first retort 4, second retort 5, three grades of absorption reactor thermallies 6 and pipelines 2.Petrol storage tank 1 top is connected with three grades of absorption reactor thermallies 6 after pipeline 2 is connected in series air water two phase separator 3, first retort 4, second retort 5 successively; Three grades of absorption reactor thermallies 6 are by three mutual leak free adsorber chambeies 61, first process chamber 62 and second process chamber 63 connect composition, adsorber chamber 61, first process chamber 62 and second process chamber, 63 equal cylinder-like structure or rectangular box structures, its bottom, chamber is equipped with the coil pipe 65 of tail end shutoff, this coil pipe 65 is provided with air extractor vent 66, the front end of adsorber chamber 61 inner coil pipes 65 extends to outside the chamber, the front end of first process chamber, 62 inner coil pipes 65 is communicated with adsorber chamber 61 top ducts, the front end of second process chamber, 63 inner coil pipes is communicated with first process chamber, 62 top ducts, and second process chamber, 63 tops are connected with detection pipeline 7; Also be placed with in adsorber chamber 61, first process chamber 62 and second process chamber 63 and handle medicament 64.Petrol storage tank 1 top duct 2 is provided with compression indicator 8.The bottom of air water two phase separator 3, first retort 4 and second retort 5 is equipped with blow-down pipe 9.
Claims (3)
1. hydrogen sulphide controlling device, comprise petrol storage tank, air water two phase separator, first retort, second retort, three grades of absorption reactor thermallies and pipeline, it is characterized in that: described petrol storage tank top is connected with three grades of absorption reactor thermallies after pipeline is connected in series air water two phase separator, first retort, second retort successively; Described three grades of absorption reactor thermallies are by three mutual leak free adsorber chambeies, first process chamber and second process chamber connect composition, described adsorber chamber, first process chamber and equal cylinder-like structure of second process chamber or rectangular box structure, its bottom, chamber is equipped with the coil pipe of tail end shutoff, this coil pipe is provided with air extractor vent, the front end of adsorber chamber inner coil pipe extends to outside the chamber, the front end of the first process chamber inner coil pipe is communicated with adsorber top of chamber pipeline, the front end of the second process chamber inner coil pipe is communicated with the first process chamber top duct, the second process chamber top is connected described adsorber chamber with the detection pipeline, also be placed with the processing medicament in first process chamber and second process chamber.
2. hydrogen sulphide controlling device according to claim 1 is characterized in that: the petrol storage tank top duct is provided with compression indicator.
3. hydrogen sulphide controlling device according to claim 1 is characterized in that: the bottom of described air water two phase separator, first retort and second retort is equipped with blow-down pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202921056U CN201753173U (en) | 2010-08-08 | 2010-08-08 | Apparatus for treating hydrogen sulfide |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010202921056U CN201753173U (en) | 2010-08-08 | 2010-08-08 | Apparatus for treating hydrogen sulfide |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201753173U true CN201753173U (en) | 2011-03-02 |
Family
ID=43620903
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010202921056U Expired - Fee Related CN201753173U (en) | 2010-08-08 | 2010-08-08 | Apparatus for treating hydrogen sulfide |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201753173U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107913648A (en) * | 2017-10-27 | 2018-04-17 | 中国石油化工股份有限公司 | A kind of pressure piping gas-liquid reactor and its processing method for oil well hydrogen sulfide treatment |
| CN108246079A (en) * | 2016-12-28 | 2018-07-06 | 天津普洛仙科技有限公司 | A kind of sulfurous gas processing unit |
| CN109847558A (en) * | 2017-11-30 | 2019-06-07 | 中国石油天然气股份有限公司 | A kind of storage tank depriving hydrogen sulphide system and technique |
-
2010
- 2010-08-08 CN CN2010202921056U patent/CN201753173U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108246079A (en) * | 2016-12-28 | 2018-07-06 | 天津普洛仙科技有限公司 | A kind of sulfurous gas processing unit |
| CN107913648A (en) * | 2017-10-27 | 2018-04-17 | 中国石油化工股份有限公司 | A kind of pressure piping gas-liquid reactor and its processing method for oil well hydrogen sulfide treatment |
| CN107913648B (en) * | 2017-10-27 | 2023-09-01 | 中国石油化工股份有限公司 | High-pressure pipeline gas-liquid reactor for treating hydrogen sulfide of oil well and treatment method thereof |
| CN109847558A (en) * | 2017-11-30 | 2019-06-07 | 中国石油天然气股份有限公司 | A kind of storage tank depriving hydrogen sulphide system and technique |
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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: 20110302 Termination date: 20130808 |