SU473378A3 - Fridge for hot high pressure process gas - Google Patents

Fridge for hot high pressure process gas

Info

Publication number
SU473378A3
SU473378A3 SU1611807A SU1611807A SU473378A3 SU 473378 A3 SU473378 A3 SU 473378A3 SU 1611807 A SU1611807 A SU 1611807A SU 1611807 A SU1611807 A SU 1611807A SU 473378 A3 SU473378 A3 SU 473378A3
Authority
SU
USSR - Soviet Union
Prior art keywords
pipe
pressure process
process gas
pipes
water
Prior art date
Application number
SU1611807A
Other languages
Russian (ru)
Inventor
Виллем Тер Хаар Леонард
Original Assignee
Шелл Интернационале Рисерч Маатсхаппий Н.В. (Фирма)
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 Шелл Интернационале Рисерч Маатсхаппий Н.В. (Фирма) filed Critical Шелл Интернационале Рисерч Маатсхаппий Н.В. (Фирма)
Application granted granted Critical
Publication of SU473378A3 publication Critical patent/SU473378A3/en

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Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10KPURIFYING OR MODIFYING THE CHEMICAL COMPOSITION OF COMBUSTIBLE GASES CONTAINING CARBON MONOXIDE
    • C10K1/00Purifying combustible gases containing carbon monoxide
    • C10K1/04Purifying combustible gases containing carbon monoxide by cooling to condense non-gaseous materials
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air
    • C01B3/34Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents
    • C01B3/36Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents
    • C01B3/363Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen by reaction of gaseous or liquid organic compounds with gasifying agents, e.g. water, carbon dioxide, air by reaction of hydrocarbons with gasifying agents using oxygen or mixtures containing oxygen as gasifying agents characterised by the burner used
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D7/00Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D7/02Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled
    • F28D7/024Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being helically coiled the conduits of only one medium being helically coiled tubes, the coils having a cylindrical configuration
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency
    • Y02P20/129Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Thermal Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Physics & Mathematics (AREA)
  • General Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Inorganic Chemistry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Industrial Gases (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Description

1one

Изобретение относитс  к холодильникам дл  технологических газов высокого давлени , полученных при осуществлении высокотемпературных нефтехимических процессов, например частичного окислени  углеводородного гырь  дл  производства синтез-газа, содержащего значительное количество сажи.The invention relates to refrigerators for high-pressure process gases obtained from high-temperature petrochemical processes, such as the partial oxidation of hydrocarbons for the production of synthesis gas containing significant amounts of carbon black.

В известном холодильнике аналогичного назначени , содержащем размещенные в цилиндрическом корпусе водоохлаждаемые спиральные змеевики, соединенные посредством газоподвод щих труб с обогреваемой трубной решеткой, а также нитательный трубопровод охлаждаюпдей воды, размещенный коаксиально со змеевикамн, охлаждение трубной рещетки и газоподвод щнх труб не  вл етс  удовлетворительным.In the well-known refrigerator of similar purpose, which contains water-cooled spiral coils placed in a cylindrical housing and connected via gas supply pipes to a heated tube sheet, as well as a cooling pipe of water cooled coaxially with coils, cooling the pipe grate and gas supply of pipes is not satisfactory.

С целью улучшени  охлаждени  трубной решетки и газоподвод щих труб трубонровод охлаждающей воды выполнен из двух концентрических труб. При этом наружна  труба в месте соединени  газоподвод щих труб с трубной решеткой окапчиваетс  центральным и по меньшей мере одним боковым эжекторами, сопла которых соединены с внутренней водонодвод щей трубой.In order to improve the cooling of the tube sheet and the gas supply pipes, the cooling water pipework is made of two concentric pipes. At the same time, the outer tube at the junction of the gas supply tubes with the tube sheet is accumulated by a central and at least one lateral ejector, the nozzles of which are connected to the inner water supply tube.

На чертеже схематично изображен холодильник дл  выcoкoтe пepaтyp югo технологнческого газа высокого давлени .FIG. 1 shows a schematic of a cooler for high-grade ultra high pressure process gas.

Холодильник содержит цилиндрический корпус I с водоохлаждаемыми спиральными змеевиками 2, соединенными посредством газоподвод щих труб 3 с трубпой решеткой 4.The refrigerator contains a cylindrical body I with water-cooled spiral coils 2 connected by means of gas supplying pipes 3 to a pipe grid 4.

Коаксиально со змеевиками размещен питательный трубопровод 5 охлаждаюп1ей воды, выполненный из двух концентрических труб 6 и 7.Coaxial with coils placed feedwater pipe 5 cooling water, made of two concentric pipes 6 and 7.

Наружна  труба 6 в месте соединен11  8 газоподвод щих труб с трубной решеткой оканчиваетс  центральнылг 9 и по крайней мере одним боковым 10 эжекторами, сопла которых 11 соединены с внутренней водоподвод щей трубой 7.The outer pipe 6 in place of the connected gas supply pipe 8 with the tube sheet ends with the central pipe 9 and at least one side 10 ejector, the nozzles of which 11 are connected to the internal water supply pipe 7.

При работе холодпльника технологический газ, имеюнип на выходе из реактора 12 температуру пор дка 1300-1400°С, давление 5- 150 ати и содержание сажи до 5 всс..о, поступает через отверсти  в трубной решетке 4 (на чертеже не показа1 ы) в газоподвод щне трубы 3 и далее - в спиральные змеевики 2.During the operation of the coldplant, the process gas, at the outlet of the reactor 12, is on the order of 1300-1400 ° C, the pressure is 5-150 atm and the soot content is up to 5 cc. About, flows through the holes in the tube sheet 4 (not shown) in gas supply pipe pipe 3 and further - into spiral coils 2.

Охлаждающа  вода поступает в питательный трубопровод 5, соответственно по паружной 6 и внутренней 7 трубам и через эжекторы 9 и 10 иодаетс  на газоподвод щие трубы 3 и в место соедннени  8 последних с трубнойThe cooling water enters the feed line 5, respectively, through the spring 6 and inner 7 pipes and through the ejectors 9 and 10 is fed to the gas supply pipes 3 and to the place of connection 8 of the latter with the pipe

решеткой 4, после чего вода омывает спиральные змеевики 2, охлажда  газ.grid 4, after which the water washes the spiral coils 2, cool the gas.

По внутренней трубе 7 охлаждающа  вода подаетс  в сопла эжекторов, посредством которых вода отсасываетс  из наружной трубы 6.Along the inner tube 7, cooling water is supplied to the ejector nozzles, by means of which water is drawn off from the outer tube 6.

Такое взаимное расположение эжекторов и концентрических водоподвод щих труб в случае прекращени  подачи охлаждаюн1ей воды по внутреннему трубопроводу обеспечивает пекоторое охлаждение с помощью воды из наружного трубопровода.Such a mutual arrangement of ejectors and concentric water supply pipes in the event of interruption of the supply of cooling water through the internal pipeline provides some cooling with the help of water from the external pipeline.

Предмет изобретени Subject invention

Холодильник дл  гор чего технологического газа высокого давлени , иапример синтез-газа , содержащий вертикальный цилиндрический корпус с водоохлаждаемымп спиральными змеевиками, соединенными посредством газоподвод щ .их труб с обогреваемой трубной рещеткой , и нитательный трубопровод охлаждающей воды, разменденный коаксиально со спиральными звеевиками, о т л и ч а ю HU-I и с   тем, что, с целью улучщени  охлаждени  т)убной решетки и газоподвод щих труб, трубопровод охлаждающей воды выиолнен из двух концентрично расноложенных труб, иричем, наружна  труба в месте соединени  газоподвод щих труб с трубной рещеткой оканчиваетс  центральным и по меньщей мере одним боковым эжекторами, сонла которых соединены с внутренней водоподвод н1ей трубой.Refrigerator for hot high-pressure process gas, such as synthesis gas, containing a vertical cylindrical body with water-cooled spiral coils connected by gas supplying them to pipes with a heated tube valve, and a nitrating line of cooling water discharged coaxially with spiral-type zheleviki about one l and HU-I, so that, in order to improve the cooling of the grate and gas supply pipes, the cooling water pipeline is made of two concentrically arranged pipes, the irish m, the outer pipe at the junction boiling gas inlet pipes with pipe terminates reschetkoy central mensche and at least one lateral ejectors, which are connected to drowsy vodopodvod n1ey inner pipe.

АBUT

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/ / / 11 (/ / / eleven (

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SU1611807A 1970-01-21 1971-01-19 Fridge for hot high pressure process gas SU473378A3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL7000812.A NL166905C (en) 1970-01-21 1970-01-21 APPARATUS FOR PREPARING AND COOLING A HYDROGEN AND CARBON MONOXIDE GAS MIX WITH A REACTION CHAMBER AND A HEAT EXCHANGER WITH AT LEAST PARTICULARLY INJURED PIPES.

Publications (1)

Publication Number Publication Date
SU473378A3 true SU473378A3 (en) 1975-06-05

Family

ID=19809144

Family Applications (1)

Application Number Title Priority Date Filing Date
SU1611807A SU473378A3 (en) 1970-01-21 1971-01-19 Fridge for hot high pressure process gas

Country Status (20)

Country Link
US (1) US3662717A (en)
JP (1) JPS5338274B1 (en)
AT (1) AT319282B (en)
BE (1) BE761460A (en)
CA (1) CA938106A (en)
CH (1) CH556797A (en)
CS (1) CS171223B2 (en)
DE (1) DE2102368C3 (en)
DK (1) DK132615C (en)
ES (1) ES387406A1 (en)
FI (1) FI53829C (en)
FR (1) FR2075714A5 (en)
GB (1) GB1340254A (en)
IE (1) IE34897B1 (en)
NL (1) NL166905C (en)
NO (1) NO132793C (en)
SE (1) SE358618B (en)
SU (1) SU473378A3 (en)
TR (1) TR16781A (en)
ZA (1) ZA71321B (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7204070A (en) * 1972-03-27 1973-10-01
NL7500554A (en) * 1975-01-17 1976-07-20 Shell Int Research HEAT EXCHANGER AND METHOD FOR COOLING HOT GASES.
GB1521094A (en) * 1975-08-27 1978-08-09 Shell Int Research Waste heat boiler
US4270493A (en) * 1979-01-08 1981-06-02 Combustion Engineering, Inc. Steam generating heat exchanger
US7301148B2 (en) 2003-04-23 2007-11-27 Battelle Memorial Institute Methods and systems for remote detection of gases
US8240366B2 (en) * 2007-08-07 2012-08-14 General Electric Company Radiant coolers and methods for assembling same
US8191617B2 (en) * 2007-08-07 2012-06-05 General Electric Company Syngas cooler and cooling tube for use in a syngas cooler
US11807822B2 (en) * 2019-02-05 2023-11-07 Saudi Arabian Oil Company Producing synthetic gas

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2790428A (en) * 1952-12-23 1957-04-30 Buttler John Allen Instantaneous steam generators
US2967515A (en) * 1956-12-21 1961-01-10 Shell Oil Co Waste-heat boiler

Also Published As

Publication number Publication date
DE2102368C3 (en) 1980-02-07
JPS5338274B1 (en) 1978-10-14
IE34897B1 (en) 1975-09-17
DE2102368B2 (en) 1979-05-10
FI53829B (en) 1978-05-02
NL7000812A (en) 1971-07-23
FI53829C (en) 1978-08-10
NO132793C (en) 1976-01-07
BE761460A (en) 1971-07-12
GB1340254A (en) 1973-12-12
DK132615C (en) 1976-05-31
DK132615B (en) 1976-01-12
CH556797A (en) 1974-12-13
US3662717A (en) 1972-05-16
SE358618B (en) 1973-08-06
CA938106A (en) 1973-12-11
ZA71321B (en) 1971-10-27
FR2075714A5 (en) 1971-10-08
NO132793B (en) 1975-09-29
CS171223B2 (en) 1976-10-29
AT319282B (en) 1974-12-10
ES387406A1 (en) 1973-05-01
NL166905B (en) 1981-05-15
DE2102368A1 (en) 1971-08-05
TR16781A (en) 1973-05-01
NL166905C (en) 1981-10-15
IE34897L (en) 1971-07-21

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