SU747401A3 - Device for adsorption purification of gases - Google Patents

Device for adsorption purification of gases Download PDF

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Publication number
SU747401A3
SU747401A3 SU721743880A SU1743880A SU747401A3 SU 747401 A3 SU747401 A3 SU 747401A3 SU 721743880 A SU721743880 A SU 721743880A SU 1743880 A SU1743880 A SU 1743880A SU 747401 A3 SU747401 A3 SU 747401A3
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USSR - Soviet Union
Prior art keywords
gas
treatment
solid
containers
gases
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SU721743880A
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Russian (ru)
Inventor
Версльюис Руланд
Шинкельшук Джэкоб
Якобус Шурман Петер
Original Assignee
Шелл Интэрнэшнл Рисерч Маатсхаппий Н.В. (Фирма)
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • B01D53/0423Beds in columns
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • B01D53/0446Means for feeding or distributing gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
    • B01D2253/10Inorganic adsorbents
    • B01D2253/104Alumina
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/20Metals or compounds thereof
    • B01D2255/207Transition metals
    • B01D2255/20723Vanadium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2255/00Catalysts
    • B01D2255/20Metals or compounds thereof
    • B01D2255/207Transition metals
    • B01D2255/20761Copper
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/30Sulfur compounds
    • B01D2257/302Sulfur oxides
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2259/00Type of treatment
    • B01D2259/40Further details for adsorption processes and devices
    • B01D2259/40083Regeneration of adsorbents in processes other than pressure or temperature swing adsorption
    • B01D2259/40086Regeneration of adsorbents in processes other than pressure or temperature swing adsorption by using a purge gas

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Gas Separation By Absorption (AREA)
  • Treating Waste Gases (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)

Abstract

1382799 Purifying gases SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ NV 1 Feb 1972 [3 Feb 1971] 4663/72 Heading B1F Apparatus for the treatment of gases containing undesirable compounds in addition to solid matter by contacting them with a gas treatment solid comprises at least two gas treating spaces of substantially the same size and shape provided within one or more columns, gas inlets to said spaces and gas outlets therefrom, and means for directing a gas to be treated alternately through each said space, each said space being provided with a plurality of containers for a gas treatment solid, which containers are so constructed of gas permeable material that they contain a system of substantially parallel gas channels and chambers for said solid, the boundaries of the gas channels being formed, at least substantially, by the walls of the adjacent chambers, which containers are so placed in said spaces that when during operation the chambers are charged with said solid, the gases to be treated will flow through the gas channels thereof. A container is exemplified in Fig. 7 in which a folded gauze 45 has inserts 49 and 50 and contains treatment solid to form alternate empty and treatment channels. The treatment of flue gas to remove sulphur oxides using metal and/or metal compound accepters of copper or banadium is referred to.

Description

54) УСТРОЙСТВО ДЛЯ АДСОРБЦИОННОЙ ОЧИСТКИ Изобретение относитс  к области адсорбционной очистки газов, например топочных газов от окислов серы. Известно устройство дл  обработки газов путем контактировани  газа с твердым веществом, состо щее из корпуса с патрубками дл  ввода и выхода газа, который вертикальна  перегородка делит на две полости, заполненные сорбентом . Недостатком известного устройства  вл етс  то, что сорбент, заполн ющий полость, быстро утрачивает проницаемость при прохождении через него газов , содержащих твердые частицы. Целью изобретени   вл етс  повышение эффективности очистки газов. Сущность изобретени  заключаетс  в том, что предлагаемое устройство. которое снабжено контейнерами-пр мо угольной формы выполненными из сетчатых пластин, расположенных параллельно вертикальным сторонам контейнеров и установленйых друг над другом на рассто нии, и направл ющими лопатками , расположенными между патрубком ввода газа и первым контейнером. Контейнеры заполн ют адсорбентом и выполн ют из газопроницаемых сет .чатых пластин таким образом, что они ГАЗОВ образуют систему параллельных открытых газовых каналов. На фиг. 1 представлено предлагаемое устройство; общий вид на фиг.2 - разрез А-А фиг. 1; на фиг. 3 - разрез Б-Б фиг. 1. Устройство состоит из корпуса 1 с патрубками ввода 2 и вывода газа 3, внутри которого помещены контейнеры . 4. Контейнеры размещены в многоугольном кожухе 5, который удерживаетс  несущими элементами 6 на цилиндрическом несущем по се 7, прикрепленном к внутренней стенке корпуса. Этот способ креплени   вл етс  достаточно герметичным, чтобы предотвратить утечку подлежащих обработке- газов вверх между стенкой корпуса и кожухом 5. Нижний слой контейнеров 4 лежит на решетке 8, котора  в свою очередь удерживаетс  несущим кольцом 9 и несущими брусь ми 10, лежащими на несущих элементах 11, прикрепленных к внутренней стенке корпуса. Эти несущие элементы 11 наход тс  выше патрубка 2 ввода. Несущие брусь  10 могут иметь отдушины дл  немедленного .уравновешивани  любого давлени , которое может развиватьс  под решеткой 8, предотвраща  тем самым неравномерность распределени  газового потока через контейнеры . Многоугольный кожух 5 имеет в различных местах горизонтальные элементы 12 жесткости, а также анкерные элементы 13, св занные с элементами 14 креплени . Многоугольный кожух 5 может быть подвешен внутри корпуса , дл  этой цели элементы б и по с 7 креп тс  в верхней част  корпуса . Между патрубком входа газа и первым слоем контейнеров размещены направл ющие лопатки 15. Кроме того, корпус имеет люки 16 и 17.54) DEVICE FOR ADSORPTION CLEANING The invention relates to the field of adsorption cleaning of gases, such as flue gases from sulfur oxides. A device for treating gases by contacting a gas with a solid substance is known, consisting of a housing with nozzles for inlet and outlet of gas, which the vertical partition divides into two cavities filled with a sorbent. A disadvantage of the known device is that the sorbent filling the cavity quickly loses its permeability when gases containing solid particles pass through it. The aim of the invention is to increase the efficiency of gas cleaning. The essence of the invention is that the proposed device. which is provided with direct-shaped containers made of mesh plates arranged parallel to the vertical sides of the containers and installed one above the other at a distance, and guide vanes located between the gas inlet nozzle and the first container. The containers are filled with an adsorbent and made of gas-permeable mesh plates in such a way that GASES form a system of parallel open gas channels. FIG. 1 shows the proposed device; General view of figure 2 - section aa of fig. one; in fig. 3 - section bb FIG. 1. The device consists of a housing 1 with nozzles of the input 2 and the output gas 3, inside which are placed the containers. 4. The containers are housed in a polygonal casing 5, which is supported by the supporting elements 6 on the cylindrical carrier along cross section 7 attached to the inner wall of the housing. This method of attachment is tight enough to prevent gases to be processed upwardly escaping between the wall of the casing and the casing 5. The bottom layer of containers 4 lies on the grid 8, which in turn is held by the supporting ring 9 and the supporting bars 10 lying on the supporting elements 11 attached to the inner wall of the housing. These carriers 11 are located above the inlet 2. Support bars 10 may have vents to immediately balance any pressure that may develop under grid 8, thereby preventing uneven distribution of the gas flow through the containers. The polygonal casing 5 has, in various places, horizontal stiffening elements 12, as well as anchor elements 13 associated with fastening elements 14. The polygonal casing 5 can be suspended inside the casing, for this purpose, the elements b and c 7 fasten to the upper part of the casing. Between the gas inlet nozzle and the first layer of containers, guide vanes 15 are placed. In addition, the housing has hatches 16 and 17.

Многоугольный кожух 5  вл етс  по форме шестиугольным и имеет три анкерные элементы 13, скрепленные с элементами 14 креплени . Шестиугольный кожух 5 заполнен контейнерами 4, поперечное сечение которых представл ет собой, например, параллелограмм с углами 60 и . Чтобы все пространство было заполнено, восемь контейнеров 4 необходимо разделить пополам .The polygonal casing 5 is hexagonal in shape and has three anchor elements 13 fastened together with fasteners 14. The hexagonal casing 5 is filled with containers 4, the cross section of which is, for example, a parallelogram with corners 60 and. For the entire space to be filled, eight containers 4 must be divided in half.

Кольцо 9 и брусь  10 образуют конструкцию , несущую контейнеры в кожухе 5. Кольцо 9, в котором закреплены брусь  10, свободно лежит на элементах 11, рассчитанных на термическое расширение.The ring 9 and the bars 10 form a structure that holds the containers in the casing 5. The ring 9, in which the bars 10 are fixed, lies freely on the elements 11 designed for thermal expansion.

Предлагаемое устройство работает следующим образом.The proposed device works as follows.

Очищаемый газ через патрубок 2 ввода поступает в корпус. 1, где направл ющие лопатки 15 измен ют направление газового потока, заставл   газы проходить через открытые газовые каналы контейнеров. Примеси, которые необходимо удалить, вступают в контакт с адсорбентом путем диффузии через газопроница€ мые стенки каналов. После прохода через р д контейнеров обработанные газы выпускаютс  из верхней части через путрубок 3 вывода.The gas to be purified through the inlet pipe 2 enters the housing. 1, where the guide vanes 15 change the direction of the gas flow, causing the gases to pass through the open gas channels of the containers. Impurities that need to be removed come into contact with the adsorbent by diffusion through the gas-permeable walls of the channels. After passing through the row of containers, the treated gases are discharged from the upper part through the nozzle 3 outlet.

В процессе удалени  из топочных газов серных окислов в окислительных услови х при повышенной температуре топочные газы контактируют с адсорбентами , улавливающими окислы серы. Предпочтительно, если адсорбент содержит металлическую медь или ванадий . Когда сорбент перегружаетс  окислами серы, он регенерируетс  восстановительным газом. В результате образованный сульфат металла разлагаетс , и металл восстанавливаетс  в металлическом виде.In the process of removing sulfur oxides from flue gases under oxidizing conditions at elevated temperatures, flue gases are in contact with adsorbents that trap sulfur oxides. Preferably, if the adsorbent contains metallic copper or vanadium. When the sorbent is overloaded with sulfur oxides, it is regenerated by the reducing gas. As a result, the metal sulphate formed decomposes and the metal is reduced in metallic form.

Таким образом, если адсорбент дезактивируетс  или его активность падает ниже некоторого минимальногоThus, if the adsorbent is deactivated or its activity falls below a certain minimum

значени , то подлежащие обработке газы проход т в следующий контейнер, а отработанный адсорбент тем временем регенерируетс  или замен етс .values, the gases to be processed go to the next container, and the spent adsorbent is regenerated or replaced in the meantime.

Дл  регенерации твердого вещества (адсорбента), заполн ющего контейнеры 4, через корпус 1 противотоком пропускаетс  регенеративный газ. Вход 18 дл  регенеративного газа выполнен в крышке 19 корпуса, а выход 20 - в нижней части корпуса, который расположен на поддоне 21. Дл  равномерного распределени  регенеративного газа по пространству корпуса в верхней части корпуса имеетс  перфорированна  пластина 22. В нижней части корпуса выполнена перфорированна  пластина 23, котора  служит дл  равномерного распределени  очищающего газа, подаваемого через выход 20 в пространство корпуса.In order to regenerate the solid (adsorbent) filling the containers 4, regenerative gas is passed through the body 1 in countercurrent. The inlet 18 for regenerative gas is made in the housing cover 19, and the outlet 20 in the lower part of the housing located on the tray 21. To evenly distribute the regenerative gas throughout the housing in the upper part of the housing there is a perforated plate 22. In the lower part of the housing there is a perforated plate 23, which serves to evenly distribute the cleaning gas supplied through the outlet 20 to the housing space.

0 в качестве восстановительного газа могут быть использованы моноокись водорода или углерода, или же смесь водородсодержащих газов.0 as a reducing gas can be used hydrogen monoxide or carbon, or a mixture of hydrogen-containing gases.

На фиг. 1 патрубки 2 и 3 расположены с одной стороны корпуса. Однако можно использовать как нижний, так и верхний патрубок дл  ввода и наоборот , в зависимости от потока, проход щего в пространстве корпуса, приQ чем направл ющие лопатки 15 дл  отклонени  газового потока могут быть установлены в различных местах в соответствии с размещением патрубка входа газового потока.FIG. 1 pipe 2 and 3 are located on one side of the housing. However, it is possible to use both the lower and the upper nozzle for the inlet and vice versa, depending on the flow in the space of the housing, when the guide vanes 15 for deflecting the gas flow can be installed in various places in accordance with the placement of the nozzle of the gas flow .

Claims (1)

1. Патент ГДР 69785, кл. В 01 D 53/02, 20.11.69 (прототип ) .1. Patent GDR 69785, cl. B 01 D 53/02, 11.20.69 (prototype).
SU721743880A 1971-02-03 1972-02-01 Device for adsorption purification of gases SU747401A3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL7101464A NL7101464A (en) 1971-02-03 1971-02-03

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SU747401A3 true SU747401A3 (en) 1980-07-23

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Application Number Title Priority Date Filing Date
SU721743880A SU747401A3 (en) 1971-02-03 1972-02-01 Device for adsorption purification of gases

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JP (1) JPS5720003B1 (en)
AU (1) AU472665B2 (en)
BE (1) BE778442A (en)
CA (1) CA976885A (en)
CS (1) CS163266B2 (en)
DE (1) DE2204702A1 (en)
FR (1) FR2126198B1 (en)
GB (1) GB1382799A (en)
IT (1) IT947210B (en)
NL (1) NL7101464A (en)
SU (1) SU747401A3 (en)
ZA (1) ZA72637B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2676635C1 (en) * 2017-07-17 2019-01-09 Общество С Ограниченной Ответственностью "Газпром Трансгаз Краснодар" Device for adsorption

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS556042U (en) * 1978-06-27 1980-01-16
JPS5945604U (en) * 1982-09-14 1984-03-26 横河電機株式会社 process controller
US4514672A (en) * 1983-04-06 1985-04-30 Ampex Corporation Adaptive apparatus and method for control
JPS61224008A (en) * 1985-03-29 1986-10-04 Yokogawa Electric Corp Sample value pi controlling device
JPS62128301A (en) * 1985-11-29 1987-06-10 Yokogawa Electric Corp Process controller
JPH01142005U (en) * 1988-03-23 1989-09-28

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE659406C (en) * 1936-12-11 1938-05-03 Hans Bischoff Dipl Ing Gas purifier
GB893329A (en) * 1957-05-16 1962-04-04 Holmes & Co Ltd W C Improvements in gas purification apparatus
US3231512A (en) * 1963-07-10 1966-01-25 Atlantic Res Corp Adsorption device
GB1094256A (en) * 1964-04-02 1967-12-06 Engelhard Ind Inc Improvements in or relating to the removal of oxides of nitrogen from gases containing them

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2676635C1 (en) * 2017-07-17 2019-01-09 Общество С Ограниченной Ответственностью "Газпром Трансгаз Краснодар" Device for adsorption

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FR2126198B1 (en) 1974-12-13
GB1382799A (en) 1975-02-05
CA976885A (en) 1975-10-28
BE778442A (en) 1972-07-25
JPS5720003B1 (en) 1982-04-26
NL7101464A (en) 1972-08-07
DE2204702A1 (en) 1972-08-10
FR2126198A1 (en) 1972-10-06
CS163266B2 (en) 1975-08-29
ZA72637B (en) 1972-10-25
AU3851472A (en) 1973-08-02
AU472665B2 (en) 1973-08-02
IT947210B (en) 1973-05-21

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