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CompetitiveTechnologiesforCO2
Reduction
in
Ethylene
Plants乙烯装置具有竞争力的CO2减排技术Information
contained
herein
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and/or
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Technology
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between
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Technology和/或其附属公司的保密和/或专有信息。所有此类信息受您、您的雇主和/或其关联公司以及Lummus
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Technology许可,不得向未授权方披露广东惠州,
Huizhou,Guangdong,
PRC.2025年11月,
November2025LUMMUSTECH
N
O
LOGY•Developstechnologysolutionsthat
make
modern
lifepossibleand
focusona
moresustainable,
low
carbonfuture开发技术解决方案使生活现代化,
聚焦更加可持续发展的低碳未来
•Oneofthe
largeststand-alonetechnology
licensingorganizations是最大的独立技术许可组织之一•Offering
includesprocesstechnologiesincleanfuels,
renewables,
petrochemicals,
polymers,gas
processingandsupplylifecycleservices,catalysts,
proprietaryequipmentanddigitalization可提供清洁燃料、可再生、石化、聚合物、气体处理等工艺技术,并提供全生命周期的服务、催化剂、专有设备和数字化•
Acquiredin2020
by
leadingprivateequityfirms,
The
Chatterjee
Groupand
Rhône
Capital2020年被领先的私人股本公司查特吉集团和罗讷资本收购Technologies技术160+LicensedUnits
许可的装置2,500+Patents专利4,100+Yearsof
IndustryLeadership业界领导地位的时间110+ASnapshotofLummusTechnology鲁玛斯技术公司概览ByTheNumbers从成就看LUMMUSTE
CH
N
O
LOGY1•Ethyleneplantsarethecore
unit
in
most
petrochemicalcomplexes乙烯装置是大多数石化一体化项目的核心单元
In2024theglobalethylenecapacityis233.8millionmetrictons.2024年乙烯全球产能约为2.338亿吨
theestimatedglobalethylenecapacitybyendof2025is246.8million
metrictons.预计至2025年底,这一数据将增长到2.468亿吨*DatacomefromSCI99.com数据来自卓创资讯•Sinceethyleneproductionisaccomplishedbythermalcracking
ofvariousfeeds
energy
consumption
is
high
由于乙烯生产是通过各种原料的热裂解来完成,具有能耗高的特点
CO2emissionsarethereforeamongstthelargestinthepetrochemicalindustry因此产生的二氧化碳是石化行业中最大的二氧化碳排放量之一
250+milliontonsofCO2eq
annualemissions(*)每年二氧化碳排放当量超2.5亿吨
(*)
Thirdlargestemitter(afterNH3
&CH3OH)
inthepetrochemical
industry是石化行业中的第三大排放源(仅次于合成氨和甲醇)•TechnologytolowertheCO2
productioniscurrentlyavailable
and
technologyto
advanceto
a
netzero
position
is
underdevelopment
目前已有技术可应用于降低二氧化碳的排放,
且二氧化碳零排放技术正在开发中•DifferentroutesareemergingforlowCarbon
Intensity
(CI)
Ethylene各种低碳强度(CI)的乙烯生产路径正在涌现•Wewillfocusontwodemonstratedtechnologiesandone
readyforcommercializationtechnologythat
when
integrated
with
the
ethylene
plantcanreduceCO2
by
morethan
50%我们将专注于两项示范技术和一项商业化技术,与乙烯装置整合,可以减少50%以上的二氧化碳•Useofmetathesischemistryfortheproductionofpropylene烯烃转化在丙烯生产中的应用•Useofisomerization&metathesischemistryforthe
productionof
butene1&
hexene-1
comonomers
异构化和歧化反应在生产1-丁烯和2-丁烯共聚单体中的应用•UtilizationofOxidativeCouplingofMethane
(OCM)
in
the
Ethylene
Plant
甲烷氧化耦合
(OCM)在乙烯装置中的应用InnovationApplied.
PerformanceDelivred.
Ethylene
Industry-
Responsibleforasignificantshare乙烯产业拥有可观的碳排放占比LUMMUSTE
CH
N
O
LOGY(*)
NexantECA2022•Ethyleneisproducedbythermalcrackingof
hydrocarbons
mixedwith
dilutionsteam
at
hightemperatures(750-900oC)
in
fired
heaters
at
lowpressuresintubularreactors乙烯是在管式反应器中,在低压高温(750-900℃)下,通过混合稀释蒸汽的烃的裂解进行生产的•Reactionis
highlyendothermic(Consumes
heat)
反应过程高度吸热(消耗热量)•Specificenergy(energyperunitweightofethylene)increasesfromethanetogasoil
从乙烷到柴油,比能(每单位乙烯的能量消耗)随之增加•Ethyleneyieldperunitweightoffeeddecreasesfromethanetogasoil
从乙烷到柴油,每单位重量原料的乙烯产率随之降低•Allenergysuppliedinthefiredheaterisnot
usedfor
reactionthoughthermalefficiency
>95%.
Excess
energy
suppliedabovethe
reaction
duty
isusedtopreheatfeedandtogenerateSHPsteam,which
isusedinthe
recovery
section尽管热效率>95%,但裂解炉中供应的所有能量并未用于反应。
超过反应所需的多余能量用于预热进料并产生回收部分所用的SHP蒸汽。•ThecrackingheatersarethelargestcontributorofCO2
productionin
the
ethylene
plant
裂解炉是乙烯装置中产生二氧化碳的最大来源•PotentialCO2
reductionmethods
include
潜在的二氧化碳减排方法包括
Maximizingtheenergytoreaction(andminimizingsteamproduction);
最大化用于反应的能量(并最小化蒸汽产量);
Changingthechemistrybytheuseofmetathesis
通过烯烃转化来改变化学组成
AlternateFuelsandheatingmethods(couplingexothermicwithendothermic
;
OCM)替代燃料和加热方式(吸放热耦合;甲烷氧化耦合)CurrentStatus
onCO2
Emissionand
Reduction
MethodsforOlefin
Production烯烃生产中的二氧化碳排放现状及减排方法InnovationApplied.
PerformanceDelivered.
3LUMMUSTE
CH
N
O
LOGYApproachesforCO2
REDUCTIONfrom
Ethylene
Plants减少乙烯装置二氧化碳排放的途径LUMMUSTECHNO
LOGY4LUMMUSTE
CH
N
O
LOGYInnovationApplied.
PerformanceDelivered.
碳捕集前燃烧纯氧燃烧压缩机驱动电气化降低能耗利用绿色能源燃气透平集成甲烷氧化耦合裂解炉采用
电加热烯烃转化-烯烃转化和共聚单体生产技术氢燃料裂解炉的空气预热技术多途径减少温室气体排放CONFIDENTIAL后燃烧5LUMMUSTE
CH
N
O
LOGYInnovationApplied.
PerformanceDelivered.
Many
PathstoGreenhouseGas
ReductionReducedEnergyConsumptionUse
ofGreenEnergyCarbonCapturePre-CombustionCrackingHeaterCombustionAirPreheatElectrificationofCompressorDriversOxy-CombustionPost-CombustionGasTurbineExhaustIntegrationMetathesis:
OCT
&
CPTOxidativeCouplingofMethaneHydrogen
FiringElectrificationofCrackingHeatersCONFIDENTIAL
6Gas
Turbine
Integration
燃气透平集成
Gasturbinegenerateselectricityandexhaust
is
usedascracking
heatercombustion
air.
燃气轮机发电,废气被用作裂解加热炉的燃烧空气。 Steamgenerationincreasesandspecificenergydecreasesbyupto30%;
蒸汽发生量增加,能量单耗降低达30%; Reducedenergyconsumptionresultsinreducedemissions降低能耗意味着碳排放降低 Commerciallyproven,availabletoday已经商业化验证,可以技术转让
Reducedenergyconsumptionresultsinreducedemissions降低能耗从而减少碳排放
Metathesis-Olefins
ConversionTechnology
andComonomer
Production
Technology歧化-烯烃转化和共聚单体生产技术 Energyneutralroutetopropyleneorcomonomerfrombutenesorpentenes利用碳四碳五烯烃采用能量中性路线生产丙烯或共聚单体 UpgradesC4sandC5stopropyleneorcomonomerat
lowerenergycost
than
recycle
cracking
or
dimerization
较于循环裂解和二聚更低能耗的升级碳四碳五为丙烯和共聚单体 Reducedenergyconsumptionresultsinreducedemissions降低能耗进而降低碳排放 Commerciallyproven,availabletoday已经商业化验证,可以技术转让Oxidative
Coupling
of
Methane
甲烷氧化耦合 Excesssteamcrackermethaneorimportedmethanefuelisconvertedto
ethylene
and
propylene
将蒸汽裂解的多余甲烷或外购甲烷转化为乙烯和丙烯 Heatfromoxidationreactionprovidesenergytoreduceemissionsfromthecracker氧化反应放出的热量可提供能量以减少乙烯装置的排放 Olefinsproducedfrommethaneatlowenergycost以较低能耗成本利用甲烷生产烯烃LummusSustainabilitySolutions鲁玛斯可持续性方案Technologies
for
a
Greener
Future–
Reduced
Energy
Consumption
绿色技术的未来-减少能量消耗Innovation
Applied.
Performance
Delivered.
CONFIDENTIAL
7LUMMUSTE
CH
N
O
LOGY
Hydrogen
Firing
氢燃料 Greenhydrogencanprovidethefuelforcrackingheaterswith
noCO2fromcombustion采用绿氢为裂解炉燃料,无二氧化碳排放 Upto
100%hydrogencanbefiredwithcurrentlyavailable
burners
目前的烧嘴技术可以采用高达100%的氢 Zeroemissionswith
100%hydrogenfuel
100%氢燃料,碳排放为零 Availabletodayforretrofitorgrassroots技术可用于改造或新项目 ElectrificationofCrackingHeaters裂解炉电气化 Greenelectricitycanreplacefossilfuelfiringasthesourceofheatrequiredforsteamcracking
reactions 采用绿电代替化石燃料作为蒸汽裂解反应的热源 Eliminatesallstackemissions消除所有烟道排放 SRT-ecommercialdemonstrationunitsuccessfullystartedup
inApr.2025
电裂解炉商业示范装置于2025年4月成功开车” Cracking
HeaterCombustionAir
Preheat裂解炉燃烧空气预热技术 Heat
recoveredintheconvectionsectionthatiscurrently
usedforsteamsuperheat
and
generationcan
be
used
to
preheat
combustion
air目前在对流段回收的用于产生和过热蒸汽的热量可用来预热燃烧空气 Firing
reductionofupto25%arepossible可以降低25%的燃烧 Reducedfuelfiredresultsinreducedstackemissions减少燃料消耗意味着烟道气排放减少 Retrofitpossiblewithout
majorconvectionsectionmodifications
可以在不需要对流段大幅改变的情况下进行改造 Readyforimplementation,currentlyinconsiderationforcrackerexpansion
project具备实施条件,目前考虑用于改扩建项目上 ElectrificationofCompressorDrivers压缩机驱动电气化 Largevariablespeedmotorscanbeusedtodrive
main
compressors大型变频电机可以用来驱动主压缩机 Motorsupto75
MWalreadyin
use
inthe
petrochemical
industry在石油化工工业上采用的最大电机为75MW Greenelectricitycanbeusedtodrivethe
motors,eliminatingtheemissions
fromfossilfuelfiringto
producesteam
采用绿电驱动电机,消除了用化石能源燃烧产生蒸汽导致的碳排放LummusSustainabilitySolutions鲁玛斯可持续性方案Technologies
for
a
Greener
Future–Use
of
Green
Energy
绿色技术的未来-利用绿色能源Innovation
Applied.
Performance
Delivered.
CONFIDENTIAL
8LUMMUSTE
CH
N
O
LOGYPreCombustion燃烧前减碳措施 HydrogenfromhydrocarbonviaSMRor
ATR通过蒸汽甲烷重整(SMR)或者
甲烷自热重整(ATR)
用烃制氢气 CO2fromshiftreactorcapturedwithconventionalaminesolvents利用传统的胺吸收捕集来自变换反应器的二氧化碳
Bluehydrogen
蓝氢OxyCombustion纯氧燃烧 Highpurityoxygenforcombustion(97+%)increasesCO2concentration
采用高纯度氧气(>97%)增加二氧化碳的浓度 Amine,membrane,oradsorptionnotrequiredforrecovery回收过程不需要胺吸收或膜分离或吸附剂 Reducedfluegasvolumereducesequipmentsize
降低烟道气体积流量,减小设备尺寸Depending
upon
localdemandandsiteconditions
potential
usesforcapturedCO2are根据当地要求和现场条件,可采用的碳捕集方法有
EnhancedOil
Recovery提高石油采收率 Sequestration封存
利用 Syngas,
Fertilizer,
Methanol,FoodGradeCO2,OxidativeCouplingof
Methane
(after
methanation)PostCombustion燃烧后减碳措施 90+%captureofcarbonfromstack可以捕获90%以上烟道气中的碳 Aminebasedsystemsarecommerciallyproven胺吸收系统已经得到商业化验证 Membraneandadsorptiontechnologiesindevelopment
膜分离和吸附技术正在开发中LummusSustainabilitySolutions鲁玛斯可持续性方案Technologies
for
a
Greener
Future–Carbon
Capture
绿色技术的未来-碳捕集Innovation
Applied.
Performance
Delivered.
CONFIDENTIAL
9Utilization合成气、化肥、甲醇、食品级二氧化碳,甲烷氧化耦合(甲烷化后)LUMMUSTE
CH
N
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LOGYCO2
Reduction
BenefitsofMetathesisto
ProducePropylene采用烯烃转化生产丙烯技术,达到二氧化碳减排LUMMUSTECHNO
LOGY10SpecificEnergyand
Relative
FiredDutyatConstant
Ethylene
Production单位乙烯产量下的比能和相对燃烧负荷Innovation
Applied.
PerformanceDelivered.
11EthaneLPGNaph-High
Naph-Low乙烷
液化石油气
轻石脑油
重石脑油EthaneLPGNaph-High
Naph-Low乙烷
液化石油气
轻石脑油重石脑油SpecificEnergyper
unitwt.ofC2H4单位重量乙烯的比能Relative
FiredDuty
perunit
C2H4单位乙烯的相对燃烧负荷1.71.61.51.41.31.21.11.00.90.81.71.61.51.41.31.21.11.00.90.8LUMMUSTE
CH
N
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LOGYRelativeSpec
ific
Fired
DutyRelativeSpecificEnergy相对燃烧负荷相对比能Cases案例Ethylene
Plant乙烯装置Ethylene
Plant+
OCT
乙烯装置+OCTAllvaluesin
kta
所有数值单位为千吨/年UltimateP/E
丙烯/乙烯0.650.65CrackingSeverity裂解强度0.650.53Feedstock(Naphtha)进料(石脑油)4,8394,630-4%Products,
kta产品Hydrogen+
FuelGas氢+燃气780787PG
Ethylene(E)聚合级乙烯1,5001,500PG
Propylene(P)聚合级丙烯9729721,3
Butadiene(BD)丁二烯280246Isobuteneproduct异丁烯产品156116Benzene(BZ)
苯273304
+11%Other
Aromatics,C7+
其他芳烃529382C9++PGO+PFOC9重芳烃+裂解汽柴油+裂解燃料油349323Total
合计4,8394,630Total
Net
E+
P净乙烯+丙烯合计2,4722,472Total
High-value
E+P+
BD+BZ
Products
高价值乙烯+丙烯+丁二烯+苯产品合计3,0253,022Total
HeaterEffluent裂解炉总产出6,0025,319
-11%InnovationApplied.
PerformanceDelivered.
12Feedand
ProductswithOCTIntegration烯烃转化技术(OCT)整合下的进料和产品LUMMUSTE
CH
N
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LOGYOCT
Integration-
Lower
CO2
Footprint烯烃转化技术整合-减少碳足迹•
EstimatedreductioninCO2
emission85KTA
估计二氧化碳排放量减少85,000吨/年•Equivalentspecific
reduction
in
CO2
perTonof
Ethylene–
0.056Ton
perTonof
Ethylene每吨乙烯的二氧化碳当量比减少量–0.056吨•
4to5%
net
CO2
reduction
二氧化碳净减排4至5%MetathesischemistryintegratedwithCrackerlowersCarbonfootprint烯烃转化与裂解炉整合,减少碳足迹Innovation
Applied.
PerformanceDelivered.
13CO2
Reduction
BenefitsofComonomerProductionTechnology采用共聚单体技术实现二氧化碳减排LUMMUSTECHNO
LOGY Hydrogen
氢 Fuel
Gas
燃气 Ethylene
乙烯
1500KTA Innovation
Applied.
PerformanceDelivered.
15Ethylene
Plant-
BaseConfiguration乙烯装置-基本配置
PGO
+
PFO裂解汽柴油+裂解燃料油ComonomerProduction共聚单体生产 Propylene
丙烯972KTABenzene
苯C7+80KTA
Butene-1Butadiene
丁二烯Polyethylene
Unit
聚乙烯单元Pygas
Hydro+
BZ裂解汽油加氢+苯RaffI
抽余液
IRaw
Mixed
C4s混合碳四Ethylene
PlantC6
NA
Recycle碳6
非芳循环C5+
Pygas碳五+
裂解汽油PE
聚乙烯1500KTA Isobutene
异丁烯Recycle
C5s
碳五回收LUMMUSTE
CH
N
O
LOGYButadiene
Extraction丁二烯抽提IsobuteneRemoval异丁烯脱除乙烯装置Naphtha石脑油抽余液
IIRaff
IICases案例Ethylene
Plant乙烯装置Ethylene
Plant+
CPT
乙烯装置+CPTAllvaluesin
kta
所有数值单位为千吨/年Feedstock(Naphtha)进料(石脑油)4,8394,920
+2%Products,
kta产品Hydrogen+
FuelGas氢+燃气780782PG
Ethylene(E)聚合级乙烯1,5001,500PG
Propylene(P)聚合级丙烯9729781,3
Butadiene(BD)丁二烯280275Isobuteneproduct异丁烯产品156158Benzene(BZ)
苯273275Butene-1丁烯085Other
Aromatics,C7+其他芳烃,
C7+529535C9++PGO+PFOC9重芳烃+裂解汽柴油+裂解燃料油348334Total
合计4,8394,920Total
Net
E+
P净乙烯+丙烯
合计2,4722,478Total
High-value
E+P+
BD+BZ+
Butene-1
Products
高价值乙烯+丙烯+丁二烯+苯+丁烯产品合计3,0253,112Total
Polyethylene
聚乙烯合计1,5001,585
+6%Total
HeaterEffluent裂解炉总产出6,0026,013
+0.2%Innovation
Applied.
PerformanceDelivered.
16Feedand
ProductswithCPT
Integration共聚单体技术整合下的进料和产品LUMMUSTE
CH
N
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LOGYCPT
Integration-
Lower
CO2
footprintCPT整合-减少碳足迹•
EstimatedreductioninCO2
emission78KTA
预计二氧化碳排放量减少78,000吨/年•Equivalentspecific
reduction
in
CO2
perTonof
Ethylene–
0.050Ton
perTonof
Ethylene每吨乙烯的单位二氧化碳减少量–0.050吨•
3to4%net
CO2
reduction
二氧化碳净减排3至4%Innovation
Applied.
PerformanceDelivered.
17MetathesischemistryintegratedwithCrackerlowersCarbonfootprint烯烃转化与裂解炉整合,减少碳足迹CO2
Reduction
BenefitsofOxidativeCouplingof
Methane甲烷氧化耦合带来的二氧化碳减排益处LUMMUSTECHNO
LOGY•Ethylene
is
produced
bythermallycrackinghydrocarbons
mixedwithdilution
steam
at
hightemperatures乙烯是在管式反应器中,
在裂解炉低压高温(750-900℃
)下,通过混合稀释蒸汽的烃热裂解产生•Reactionis
highlyendothermic
(Consumes
heat)
反应过程高度吸热(消耗热量)•Inan
Ethylene
Plantalmostall
CO2
isgenerated
in
the
fired
heaters
在乙烯装置中,几乎所有的二氧化碳都通过加热炉产生
Burning
methane
byproductfromcracking燃烧裂解产生甲烷副产品•Potential
Reduction
Method
潜在减排方法
Couplinganexothermic
processwithendothermiccracking–
OCM
放热过程和吸热裂解耦合-甲烷氧化耦合•
Oxidative
Coupling
of
Methane
Reaction
甲烷氧化耦合反应
2CH4
+O2
C2
H4
+2H2O
+
heat
加热•
Gemini
TMOCM
process
by
Lummus
鲁姆斯拥有的GeminiTM
OCM工艺Innovation
Applied.
PerformanceDelivered.
19(750-900oC)
in
fired
heaters
at
low
pressures
in
tubular
reactorsEthylene
PlantCO2
Emissions乙烯装置二氧化碳排放LUMMUSTE
CH
N
O
LOGYInnovationApplied.
PerformanceDelivered.
20SCU
FuelGas蒸汽裂解富甲烷气Oxygen氧气C2
/C3
Recycle
碳2/碳3回收METHANATOR甲烷化器OCM
REACTOR甲烷氧化耦合反应器HEATRECOVERY热回收Recycle
heaterreplacedby
OCM
reactor,reducing
firing循环炉被甲烷氧化耦合反应器取代,减少燃烧负荷CO2
recoveredandconvertedto
products二氧化碳被回收并转化为产品PGCOMPR.压缩CO2REMOVAL二氧化碳脱除WaterinsteadofCO2
emission排放水而不是二氧化碳OCM
Block
Flow甲烷氧化耦合流程框图C2+
ProductSCU碳二+去蒸汽裂解产品WaterEffluent出水CO2
Recycle
二氧化碳循环LUMMUSTE
CH
N
O
LOGYC1
Recycle碳1循环CRYOSEPS低温分离DRYING干燥OCM
Integration-
Lower
CO2
footprint甲烷氧化耦合整合-减少碳足迹•OCM
replacesthe
recycle
heatercracking
甲烷氧化耦合代替循环裂解
Converting92
kta
of
fuel
gas
可转化92,000吨/年燃气
Reduces
CO2
emission
from
firing
248kta,
12%减少燃烧产生的二氧化碳排放量24.8万吨/年,12%OCMchemistryintegratedwithCrackerlowers
Carbon
footprint甲烷氧化耦合与裂解装置整合,减少碳足迹•OCM
produces
57kta
more
ethylene
from
the
excess
fuel
gas,
reduces
CO2
4%
甲烷氧化耦合从过剩燃料气中生产了额外5.7万吨/年乙烯,减少了4%的二氧化碳•Reduction
in
specific
CO2
per
Ton
of
Ethylene
–
0.16Ton
per
Ton
of
Ethylene
–
12.3%
of
the
total
ethyleneproductionCO2
footprint每吨乙烯的单位二氧化碳排放量减少——0.16吨——占乙烯生产总二氧化碳排放量的12.3%InnovationApplied.
PerformanceDelivered.
21LUMMUSTE
CH
N
O
LOGYSummary总结LUMMUSTECHNO
LOGY•
Generationofhydrogentoincreasethefuelfiredinthecracking
heaters
to
100%
hydrogen
产生氢气以将裂解炉中燃烧的燃料替换为100%氢气•Totalelectrificationoftheethylene
plantincludingalldrivers
andthe
cracking
heaters.This
cannot
be
put
into
practiceyet
butcommercializationofthefirstSRT-efurnaceisnearlyready包括所有驱动器和裂解炉在内的乙烯装置全部电气化。目前尚不能付诸实践,但第一台SRT-e炉的商业化已接近完成•
RecoveryofCO2
fromthecrackingheaterfluegasanddisposalofthe
recovered
CO2
eitherbysequestrationor
conversion
to
methaneforuseinthe
OCM
process从裂解炉烟道气中回收二氧化碳,并通过封存或转化成用于甲烷氧化耦合工艺的甲烷来处理回收的二氧化碳•Combustion
AirPreheating燃烧空气预热•
Ethyleneplantpartialelectrification
乙烯装置部分电气化•AdditionofOCMchemistrytothecomplex在联合装置中增加甲烷氧化耦合装置•AdditionofOCT/CPTchemistrytothecomplex在联合装置中增加烯烃转化技术/共聚单体技术CO2
emissions
can
be
reduced
or
eliminated
from
ethylene
plants
乙烯装置排放的二氧化碳可以减少或消除CO2
canbereducedby
以下方法可减少二氧化碳:InnovationApplied.
PerformanceDelivered.
23LowerCO2
EmissionsSummaryofKey
Points二氧化碳减排关键点总结CO2
canbeessentiallyeliminatedby
以下方法可基本消除二氧化碳:LUMMUSTE
CH
N
O
LOGYLowCarbon
Emission
PXCrystallizationTechnology低碳排放的PX结晶分离技术Information
contained
herein
is
confidential
and/or
proprietaryto
Lummus
Technology
and/or
its
affiliates.All
such
information
is
protected
bythe
relevant
agreements,
including
confidentiality
and
limited
use
agreements,
between
you,
your
employer
and/or
its
affiliates,
and
LummusTechnologyor
itsaffiliates.
The
information
herein
mayonly
be
used
in
accordance
with
those
agreements,
and
is
not
to
be
disclosed
to
unauthorized
parties
without
permission
of
Lummus
Technology.本信息是Lummus
Technology和/或其附属公司的保密和/或专有信息。所有此类信息受您、您的雇主和/或其关联公司以及Lummus
Technology或其关联公司之间的相关协议保护,包括保密和限制使用协议。此处的信息只能根据这些协议使用,未经Lummus
Technology许可,不得向未授权方披露广东惠州,
Huizhou,Guangdong,
PRC.2025年11月,
November2025LUMMUSTECH
N
O
LOGY•CommercialExperience
业绩•Overall
ProcessScheme
总流程•Geel
PXOverview基尔PX工厂概览•Benefits
Summary优势总结WhySelectDouble
ReslurryCrystallization为何选择两段重浆化结晶工艺InnovationApplied.
PerformanceDelivered.
25Agenda议程LUMMUSTE
CH
N
O
LOGYContinuouslyimprovedforover50years
50多年对技术不断改进和完善Lowestcapex,opexandenvironmentalemissions最低的投资、操作成本和环境排放Energyefficient低能耗Abilitytodebottleneckorexpand可用于现有装置去瓶颈或扩建Reliable可靠性高Doublereslurrycrystallization
istheCLEAR
choice两段重浆化结晶是最佳选择InnovationApplied.
PerformanceDelivered.
26LUMMUSTE
CH
N
O
LOGY•2022.2Theexecutionguidelineforupgradingtheprojects
in
majorareas
ofenergy-intensive
industriestosaveenergyandreducecarbonemission
issuedby
NDRCwheretheattachment3forPX
indicatesencouragingthedevelopmentandapplicationofthedoublereslurrycrystallizationprocess.2022.2国家发改委颁布《高耗能行业重点领域节能降碳改造升级实施指南》,其中关于PX的附件3提到“加大两段重浆化结晶工艺技术研发应用”。•2022.8ImplementationPlanforCarbon
Peaking
inthe
Industrial
Field
issued
whichmentionspromotingelectrificationofi
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