CN104295908A - CO2 quality control and conveying pipe corrosion control method - Google Patents

CO2 quality control and conveying pipe corrosion control method Download PDF

Info

Publication number
CN104295908A
CN104295908A CN201410499716.0A CN201410499716A CN104295908A CN 104295908 A CN104295908 A CN 104295908A CN 201410499716 A CN201410499716 A CN 201410499716A CN 104295908 A CN104295908 A CN 104295908A
Authority
CN
China
Prior art keywords
quality control
conveying pipe
content
corrosion
impurity
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.)
Pending
Application number
CN201410499716.0A
Other languages
Chinese (zh)
Inventor
蒋秀
屈定荣
刘小辉
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China Petroleum and Chemical Corp
Sinopec Qingdao Safety Engineering Institute
Original Assignee
China Petroleum and Chemical Corp
Sinopec Qingdao Safety Engineering Institute
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by China Petroleum and Chemical Corp, Sinopec Qingdao Safety Engineering Institute filed Critical China Petroleum and Chemical Corp
Priority to CN201410499716.0A priority Critical patent/CN104295908A/en
Publication of CN104295908A publication Critical patent/CN104295908A/en
Pending legal-status Critical Current

Links

Landscapes

  • Preventing Corrosion Or Incrustation Of Metals (AREA)

Abstract

The invention relates to a CO2 quality control and conveying pipe corrosion control method. The method mainly solves the problems that the retardation time is long and corrosion risks of a conveying pipe are big in the CO2 quality control in the prior art. By the adoption of the CO2 quality control and conveying pipe corrosion control method, an instrument for measuring impurity content in CO2 online is installed at the inlet position of the CO2 conveying pipe, and when the content of any impurity in the CO2 entering the conveying pipe is higher than a quality control value but lower than a high limit value, the instrument and a monitor center will automatically give an alarm, and a pipe conveying system starts a corrosion inhibitor processing system. According to the technical scheme, when the content of any impurity in the CO2 entering the conveying pipe is higher than the high limit value, the instrument and the monitor center will automatically give an alarm, and the pipe conveying system automatically cut the CO2 away, so that the problems are well solved, and the method can be used for carbon dioxide quality control and conveying pipe corrosion control.

Description

Carbon dioxide quality control and conveyance conduit process for corrosion control thereof
Technical field
The present invention relates to a kind of carbon dioxide quality control and conveyance conduit process for corrosion control thereof.
Background technique
Global warming has become the focus of World Focusing, CO 2plugging Technology Applied (CCS) comprises the catching of carbon, transports, and store or use, oneself is put into the technology emphasis special campaigns of state control greenhouse gas emission and mitigation of climate change.CO 2transport is CO 2from place of capture to storage place or make the intermediate hub of land used.Utilize pipeline transport to storing ground or making land used normally carry CO on a large scale 2most economical, feasible method.CN201210191439.8 discloses a kind of carbon dioxide booster transportation apparatus, the carbon dioxide storage tank of this device is connected with liquid-gas separator input end, liquid-gas separator output terminal is connected with carbon dioxide booster pump input end, carbon dioxide booster pump first output terminal leads to high-pressure carbon dioxide output terminal by heat exchanger and auxiliary heating case, is also connected with carbon dioxide storage tank by high-pressure electric control servo valve.Carbon dioxide booster pump second output terminal is connected with liquid-gas separator output terminal, carbon dioxide storage tank respectively, and carbon dioxide booster pump the 3rd output terminal is connected with carbon dioxide storage tank by low-pressure electric controlled servo valve, canned motorpump.
The CO of industrial discharge 2generally deviate from after water and various impurity through purified treatment and carry again, but the thorough extensive CO of purifying 2bring technological challenge and uneconomical, therefore, the CO of Cemented filling 2all containing certain impurity in gas, the existence of these impurity causes CO 2the risk of corrosive pipeline.Work as CO 2when pipeline has elutriation to go out, the corrosion rate of carbon steel piping can reach about 20mm/y; If CO 2in there is SO 2, NO 2or O 2, the corrosion condition of pipeline is more complicated.Therefore, control to enter CO 2each impurity content of pipeline is the important measures avoiding pipeline to be corroded.
In addition, CO is entered 2the CO of pipeline 2quality is also subject to having a strong impact on of the treatment process of upstream process factory, can not keep constant.Once the treatment process fluctuation for the treatment of plant, enter the CO of pipeline 2middle impurity content just may exceed level of control.The method that existing gaseous mass controls is to CO in specific time interval 2gas is sampled, then analyzes in laboratory, to discovery CO 2makings whether meet quality control requirement life period retardation phenomenon, to the gaseous mass during double sampling without any surveillance and control measure.
The present invention solves this problem targetedly.
Summary of the invention
Technical problem to be solved by this invention is CO in prior art 2quality control there is longer lag time, problem that conveyance conduit corrosion risk is larger, a kind of new carbon dioxide quality control and conveyance conduit process for corrosion control thereof are provided.The method is used for, in carbon dioxide quality control and conveyance conduit corrosion control thereof, having CO 2the advantage that quality control lag time is very short, conveyance conduit corrosion risk is less.
For solving the problem, the technical solution used in the present invention is as follows: a kind of carbon dioxide quality control and conveyance conduit process for corrosion control thereof, at CO 2on-line measurement CO is installed in conveyance conduit ingress 2the instrument of middle impurity content, when entering the CO of conveyance conduit 2in the content of any one impurity higher than quality control value lower than ceiling value time, the equal automatic alarm of instrument and Surveillance center, pipe-line transportation system starts corrosion inhibitor processing system; When entering the CO of conveyance conduit 2in the content of any one impurity higher than ceiling value time, the equal automatic alarm of instrument and Surveillance center, pipe-line transportation system cuts out CO automatically 2.
In technique scheme, preferably, described impurity comprises water, SO 2, NO 2and O 2.
The present invention adopts the method for on-line monitoring, once CO 2quality do not meet quality control requirement, can make an immediate response and take measures, avoiding the corrosion of pipeline, achieving good technique effect.
Below by embodiment, the invention will be further elaborated, but be not limited only to the present embodiment.
Embodiment
[embodiment 1]
At CO 2entrance place installs can measure CO 2middle water, SO 2, NO 2and O 2the instrument of content, on-line monitoring CO 2makings, by setting CO 2cO under delivery temperature pressure condition 2in the quality control level of each impurity, as water content C1, SO 2content C2, NO 2content C3 and O 2content C4.Once enter the CO of pipeline 2the contents level of middle any one impurity higher than setting value, the equal automatic alarm of instrument and Surveillance center.This illustrates CO 2disposal quality defective, exist and cause the risk of corrosive pipeline.
If the water content of actual measurement is greater than CI1, or SO 2content is greater than CI2, or NO 2content is greater than CI3 or O 2content is greater than CI4, and pipe-line transportation system blocks CO automatically 2enter pipeline, CO 2need to re-start process, wherein C1<CI1, C2<CI2, C3<CI3, C4<CI4.If the water content of actual measurement is between C1 ~ CI1, or SO 2content is between C2 ~ CI2, or NO 2content is between C3 ~ CI3 or O 2content between C4 ~ CI4, CO 2can continue to enter pipeline, but corrosion inhibitor processing system need be started, avoid CO 2conveyance conduit is corroded, and this can be avoided adding corrosion inhibitor to pipe interior continuously, increases the utilization ratio of corrosion inhibitor and reduces corrosion control cost, and ensureing the safety of pipeline.

Claims (2)

1. carbon dioxide quality control and a conveyance conduit process for corrosion control thereof, at CO 2on-line measurement CO is installed in conveyance conduit ingress 2the instrument of middle impurity content, when entering the CO of conveyance conduit 2in the content of any one impurity higher than quality control value lower than ceiling value time, the equal automatic alarm of instrument and Surveillance center, pipe-line transportation system starts corrosion inhibitor processing system; When entering the CO of conveyance conduit 2in the content of any one impurity higher than ceiling value time, the equal automatic alarm of instrument and Surveillance center, pipe-line transportation system cuts out CO automatically 2.
2. carbon dioxide quality control and conveyance conduit process for corrosion control thereof according to claim 1, is characterized in that described impurity comprises water, SO 2, NO 2and O 2.
CN201410499716.0A 2014-09-25 2014-09-25 CO2 quality control and conveying pipe corrosion control method Pending CN104295908A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410499716.0A CN104295908A (en) 2014-09-25 2014-09-25 CO2 quality control and conveying pipe corrosion control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410499716.0A CN104295908A (en) 2014-09-25 2014-09-25 CO2 quality control and conveying pipe corrosion control method

Publications (1)

Publication Number Publication Date
CN104295908A true CN104295908A (en) 2015-01-21

Family

ID=52315756

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410499716.0A Pending CN104295908A (en) 2014-09-25 2014-09-25 CO2 quality control and conveying pipe corrosion control method

Country Status (1)

Country Link
CN (1) CN104295908A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105822901A (en) * 2016-05-29 2016-08-03 济南科慧页岩化工技术有限公司 Pipeline for capturing and utilizing CO2 produced through metallurgy and laying working method of pipeline

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08178186A (en) * 1994-12-22 1996-07-12 Iwatani Internatl Corp Control method for transfer of liquefied gas to liquefied gas using apparatus
CN1338628A (en) * 2000-08-10 2002-03-06 同济大学 Monitor and alarm system for multi-component gas
CN101358687A (en) * 2007-08-01 2009-02-04 上海正帆超净技术有限公司 Gas safety conveying method
US20110220207A1 (en) * 2010-03-09 2011-09-15 Bronner Raymond A Solenoid gas meter mounting bracket valve
CN102872689A (en) * 2012-08-20 2013-01-16 中国计量学院 Infrared differential spectroscopy-based biogas detection and purification control system
CN203489006U (en) * 2013-09-29 2014-03-19 淄博安益矿用设备有限公司 Safe conveying system for coalbed methane

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08178186A (en) * 1994-12-22 1996-07-12 Iwatani Internatl Corp Control method for transfer of liquefied gas to liquefied gas using apparatus
CN1338628A (en) * 2000-08-10 2002-03-06 同济大学 Monitor and alarm system for multi-component gas
CN101358687A (en) * 2007-08-01 2009-02-04 上海正帆超净技术有限公司 Gas safety conveying method
US20110220207A1 (en) * 2010-03-09 2011-09-15 Bronner Raymond A Solenoid gas meter mounting bracket valve
CN102872689A (en) * 2012-08-20 2013-01-16 中国计量学院 Infrared differential spectroscopy-based biogas detection and purification control system
CN203489006U (en) * 2013-09-29 2014-03-19 淄博安益矿用设备有限公司 Safe conveying system for coalbed methane

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
左甜等: "临界CO2输送管道的腐蚀研究进展", 《石油化工腐蚀与防护》 *
蒋秀等: "超临界CO2管道输送与安全", 《油气储运》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105822901A (en) * 2016-05-29 2016-08-03 济南科慧页岩化工技术有限公司 Pipeline for capturing and utilizing CO2 produced through metallurgy and laying working method of pipeline
CN105822901B (en) * 2016-05-29 2018-11-13 济南科慧页岩化工技术有限公司 It is a kind of to trap, metallurgy is utilized to generate CO2Pipeline and its be laid with working method

Similar Documents

Publication Publication Date Title
US7208117B2 (en) Automated process for inhibiting corrosion in an inactive boiler containing an aqueous system
EP2579018A1 (en) Detection system and humidity detection method for detecting volatile organic compound
WO2017089846A1 (en) Process for feeding an inhibitor into a gas pipeline for preventing gas hydrate formation
WO2016101914A1 (en) Station control system and method for unattended lng gas station
US11274049B2 (en) Methods and systems for optimizing corrosion and scale inhibitor injection rates in process plants
CN204214688U (en) A kind of gas phase separation sampling system of hydrolysis of urea reactor
CN103803583B (en) System and the control method thereof of ammonia are produced in a kind of ammoniacal liquor evaporation
CN104295908A (en) CO2 quality control and conveying pipe corrosion control method
CN104731122A (en) pH detection and adjustment method for ammonium nitrate solution for emulsion explosive production
CN112875830A (en) Automatic control method and system for pH value of inlet of secondary reverse osmosis system
CN202327650U (en) Emergency spray device for liquid ammonia leakage
CN103157376A (en) SNCR and SCR (Selective Non-catalytic Reduction and Selective Catalytic Reduction) combined reducing agent storage and preparation system
CN109647135A (en) Collecting carbonic anhydride purification devices technical grade finished product prepares detection system
CN209927761U (en) Online real-time detection device for hydrocarbon dew point of gas pipeline
CN204310865U (en) For the sewage toxicity early warning system of Sewage Plant
CN209841751U (en) Online real-time detection device for water dew point of gas pipeline
CN109163216B (en) Safe intelligent liquid ammonia vaporization system
CN203824818U (en) Extraction type fume-emission gaseous pollutant-continuous monitoring measuring dewatering system
US9772061B2 (en) Examination process for the in situ determination of rate of feeding an inhibitor into a gas pipeline for preventing hydrate formation
CN207036569U (en) A kind of pipe-line system gas pressure test system of petrochemical industry station project
CN106090946B (en) A kind of torch condensation water recovery system
CN104492290A (en) Low-concentration coal gas blending device for coal mine
CN204294131U (en) Coal mine light concentration mash gas blending device
CN203908827U (en) Corrosive gas sampling device
CN103471873A (en) Liquid concentrated sampling cabinet

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication

Application publication date: 20150121

RJ01 Rejection of invention patent application after publication