CN110257099A - A method of freshening being carried out to dross using coke drum - Google Patents

A method of freshening being carried out to dross using coke drum Download PDF

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Publication number
CN110257099A
CN110257099A CN201910544577.1A CN201910544577A CN110257099A CN 110257099 A CN110257099 A CN 110257099A CN 201910544577 A CN201910544577 A CN 201910544577A CN 110257099 A CN110257099 A CN 110257099A
Authority
CN
China
Prior art keywords
dross
coke drum
freshening
coke
carrying
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
CN201910544577.1A
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Chinese (zh)
Inventor
袁培忠
李民举
江海伟
柴永胜
李勇
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.)
JIANGSU XINHAI PETROCHEMICAL GROUP CO Ltd
Original Assignee
JIANGSU XINHAI PETROCHEMICAL GROUP CO Ltd
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 JIANGSU XINHAI PETROCHEMICAL GROUP CO Ltd filed Critical JIANGSU XINHAI PETROCHEMICAL GROUP CO Ltd
Priority to CN201910544577.1A priority Critical patent/CN110257099A/en
Publication of CN110257099A publication Critical patent/CN110257099A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B55/00Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G9/00Thermal non-catalytic cracking, in the absence of hydrogen, of hydrocarbon oils
    • C10G9/005Coking (in order to produce liquid products mainly)

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  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Coke Industry (AREA)

Abstract

The present invention relates to a kind of methods for carrying out freshening to dross using coke drum, including following step S1: starting dross pump conveys dross into coke drum along 10 meters of dross valves;S2: dross enters coke drum after twenty minutes, and starting water pump confirms that coke cooling water into after coke drum, is closed to steam valve toward coke drum water supply;S3: by heating up to coke drum, temperature rises to 450 DEG C -500 DEG C and carries out freshening to dross;Daily freshening amount can be greatly improved using this method, company dross inventory is effectively relieved, and strong reduction environmental protection pressure has reached desired effect.

Description

A method of freshening being carried out to dross using coke drum
Technical field
The present invention relates to a kind of dross freshening methods, are specifically related to a kind of side for carrying out freshening to dross using coke drum Method.
Background technique
Workshop dross inventory is high, and there are immense pressure, daily 18 tons of the freshenings in coking workshop for environmental protection operation facility Amount, cannot effectively alleviate current driving force workshop dross inventory problem and environmental protection pressure.Coking dross freshening flowmeter limitation, It is returned back out in the freshening later period existing, it will be apparent that pipeline vibration, there are security risks;So designing a kind of application to solve the above-mentioned problems The method that coke drum carries out freshening to dross is just particularly important.
Summary of the invention
The present invention can stop dross freshening after coke drum freshening temperature is down to 290 DEG C immediately, avoid the occurrence of dross in coke The case where cannot being reacted completely in charcoal tower.During dross blowback is refined, it must contact, prevent with power houses in time when changing process Pump builds the pressure;A kind of method carrying out freshening to dross using coke drum is provided.
In order to solve the above technical problems, the present invention provides it is a kind of using coke drum to dross carry out freshening method, It is characterized by comprising following steps:
S1: starting dross pump conveys dross into coke drum along 10 meters of dross valves;
S2: dross enters coke drum after twenty minutes, starting water pump toward coke drum water supply, confirm coke cooling water into after coke drum, It closes to steam valve;
S3: by heating up to coke drum, temperature rises to 450 DEG C -500 DEG C and carries out freshening to dross.
Further, post personnel observes 10 meters of dross valve feedwater line site pressure expression conditions, pressure in the step S1 Power rise after open water valve, give vapour amount keep 2.5-3t/h.
Further: in the step S2, confluent maintains 25t/h or so, and dross freshening amount keeps 45t/h, and The rear stopping dross pump at freshening 15 minutes or so, and close dross valve.
Further: in the step S3, observe top of coke tower pressure and temperature, pressure rise it is too fast when can reduce to Water, after temperature is down to 290 DEG C, it is necessary to stop dross freshening at once.
After adopting the above structure, the present invention can stop dross freshening after coke drum freshening temperature is down to 290 DEG C immediately, keep away Exempt from the case where dross cannot react completely in coke drum occur.It, must be in time and dynamic when changing process during dross blowback is refined The connection of power workshop, prevents pump from building the pressure;And daily freshening amount can be greatly improved using this method, company's dross library is effectively relieved It deposits, strong reduction environmental protection pressure has reached desired effect.
Specific embodiment
The present invention provides a kind of methods for carrying out freshening to dross using coke drum:
S1: starting dross pump conveys dross into coke drum along 10 meters of dross valves;
S2: dross enters coke drum after twenty minutes, starting water pump toward coke drum water supply, confirm coke cooling water into after coke drum, It closes to steam valve;
S3: by heating up to coke drum, temperature rises to 450 DEG C -500 DEG C and carries out freshening to dross.
In above-mentioned step S1, post personnel observes 10 meters of dross valve feedwater line site pressure expression conditions, and pressure rises Afterwards open water valve, give vapour amount keep 2.5-3t/h.
In above-mentioned step S2, confluent maintains 25t/h or so, and dross freshening amount keeps 45t/h, and divides in freshening 15 The rear stopping dross pump of clock or so, and close dross valve.
In above-mentioned step S3, top of coke tower pressure and temperature is observed, pressure can reduce confluent, temperature when rising too fast After being down to 290 DEG C, it is necessary to stop dross freshening at once.
In conclusion the present invention can stop dross freshening after coke drum freshening temperature is down to 290 DEG C immediately, avoid the occurrence of The case where dross cannot react completely in coke drum.It, must timely and power houses when changing process during dross blowback is refined Connection prevents pump from building the pressure;And daily freshening amount can be greatly improved using this method, company dross inventory is effectively relieved, has The reduction environmental protection pressure of power, has reached desired effect.

Claims (4)

1. a kind of method for carrying out freshening to dross using coke drum, it is characterised in that: the following steps are included:
S1: starting dross pump conveys dross into coke drum along 10 meters of dross valves;
S2: dross enters coke drum after twenty minutes, and starting water pump confirms that coke cooling water into after coke drum, is closed toward coke drum water supply To steam valve;
S3: by heating up to coke drum, temperature rises to 450 DEG C -500 DEG C and carries out freshening to dross.
2. a kind of method for carrying out freshening to dross using coke drum according to claim 1, it is characterised in that: described In step S1, post personnel observe 10 meters of dross valve feedwater line site pressure expression conditions, pressure rise after open water valve, give vapour Amount keeps 2.5-3t/h.
3. a kind of method for carrying out freshening to dross using coke drum according to claim 1, it is characterised in that: described In step S2, confluent maintains 25t/h or so, and dross freshening amount keeps 45t/h, and rear stopping was floating at freshening 15 minutes or so Pulp pump, and close dross valve.
4. a kind of method for carrying out freshening to dross using coke drum according to claim 1, it is characterised in that: described In step S3, top of coke tower pressure and temperature is observed, pressure can reduce confluent when rising too fast must after temperature is down to 290 DEG C It must stop dross freshening at once.
CN201910544577.1A 2019-06-21 2019-06-21 A method of freshening being carried out to dross using coke drum Pending CN110257099A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910544577.1A CN110257099A (en) 2019-06-21 2019-06-21 A method of freshening being carried out to dross using coke drum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910544577.1A CN110257099A (en) 2019-06-21 2019-06-21 A method of freshening being carried out to dross using coke drum

Publications (1)

Publication Number Publication Date
CN110257099A true CN110257099A (en) 2019-09-20

Family

ID=67920397

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910544577.1A Pending CN110257099A (en) 2019-06-21 2019-06-21 A method of freshening being carried out to dross using coke drum

Country Status (1)

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CN (1) CN110257099A (en)

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1803654A (en) * 2005-12-08 2006-07-19 南京工业大学 Oil-containing dross dehydration process
CN201500672U (en) * 2009-08-14 2010-06-09 山东三维石化工程股份有限公司 Oil refining enterprise flotation dross treating device
CN102951744A (en) * 2011-08-31 2013-03-06 中国石油化工股份有限公司 Oil-containing water-enriched scum dehydration treatment method
CN105271466A (en) * 2014-07-11 2016-01-27 中国石油化工股份有限公司 Oily scum dehydrator and preparation method thereof
CN205346894U (en) * 2015-11-28 2016-06-29 万达集团股份有限公司 Oil slick, dross processing system
CN206328341U (en) * 2016-12-29 2017-07-14 上海彧丰信息科技有限公司 A kind of oil plant scum silica frost processing system containing delayed coking unit

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1803654A (en) * 2005-12-08 2006-07-19 南京工业大学 Oil-containing dross dehydration process
CN201500672U (en) * 2009-08-14 2010-06-09 山东三维石化工程股份有限公司 Oil refining enterprise flotation dross treating device
CN102951744A (en) * 2011-08-31 2013-03-06 中国石油化工股份有限公司 Oil-containing water-enriched scum dehydration treatment method
CN105271466A (en) * 2014-07-11 2016-01-27 中国石油化工股份有限公司 Oily scum dehydrator and preparation method thereof
CN205346894U (en) * 2015-11-28 2016-06-29 万达集团股份有限公司 Oil slick, dross processing system
CN206328341U (en) * 2016-12-29 2017-07-14 上海彧丰信息科技有限公司 A kind of oil plant scum silica frost processing system containing delayed coking unit

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
唐华跃等: "延迟焦化处理炼油厂浮渣", 《石油炼制与化工》 *

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Application publication date: 20190920

RJ01 Rejection of invention patent application after publication