SU659071A3 - Method of obtaining gases - Google Patents

Method of obtaining gases

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Publication number
SU659071A3
SU659071A3 SU742001184A SU2001184A SU659071A3 SU 659071 A3 SU659071 A3 SU 659071A3 SU 742001184 A SU742001184 A SU 742001184A SU 2001184 A SU2001184 A SU 2001184A SU 659071 A3 SU659071 A3 SU 659071A3
Authority
SU
USSR - Soviet Union
Prior art keywords
gas
impurities
water
stream
amount
Prior art date
Application number
SU742001184A
Other languages
Russian (ru)
Inventor
Эрик Набер Яаап
Ван Ос Джордж
Original Assignee
Шелл Интернэшнл Рисерч Маатсхаппий Б.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 Интернэшнл Рисерч Маатсхаппий Б.В. (Фирма) filed Critical Шелл Интернэшнл Рисерч Маатсхаппий Б.В. (Фирма)
Application granted granted Critical
Publication of SU659071A3 publication Critical patent/SU659071A3/en

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Classifications

    • 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
    • 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
    • C01B3/50Separation of hydrogen or hydrogen containing gases from gaseous mixtures, e.g. purification
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2203/00Integrated processes for the production of hydrogen or synthesis gas
    • C01B2203/04Integrated processes for the production of hydrogen or synthesis gas containing a purification step for the hydrogen or the synthesis gas
    • C01B2203/0465Composition of the impurity
    • C01B2203/0485Composition of the impurity the impurity being a sulfur compound

Description

1one

Изобретение относитс  к способам получени  газов и может найти применение в технологических процессах получени  водорода .The invention relates to methods for producing gases and may find application in technological processes for producing hydrogen.

Известен способ получени  газов, содержащих водород и окись углерода, путем неполного сжигани  углеводородов с последующей очисткой гор чего газа пропусканием через циклон, насыщением газа водой и промывкой в пенном слое при 30 40°С .A method of producing gases containing hydrogen and carbon monoxide is known by incompletely burning hydrocarbons, followed by purifying the hot gas by passing through a cyclone, saturating the gas with water, and washing in the foam layer at 30-40 ° C.

Недостатками этого способа  вл ютс  сложность технологического оформлени  процесса , а также наличие больщого количества сточных вод.The disadvantages of this method are the complexity of the technological design of the process, as well as the presence of a large amount of wastewater.

Наиболее близок к предлагаемому изобретению способ получени  газов, содержащих водород и/или окись углерода, включающий неполное сжигание углеводородов, охлаждение продуктов сжигани  до температуры не ниже 200-210°С и очистку их от твердых частиц в циклоне, а затем водной промывкой в скрубберах 2.Closest to the proposed invention is a method of producing gases containing hydrogen and / or carbon monoxide, including incomplete combustion of hydrocarbons, cooling the products of combustion to a temperature not lower than 200-210 ° C and purifying them from solid particles in a cyclone, and then water washing in scrubbers 2 .

Однако при таком способе частицы золы , захваченные водой, вывод тс  из процесса в виде водной суспензии золы, которую из-за невозможности утилизации приходитс  сбрасывать в промыщленные стоки , загр зн   окружающую среду.However, with this method, ash particles trapped in water are removed from the process in the form of an aqueous suspension of ash, which, due to the impossibility of disposal, has to be discharged into industrial drains, polluting the environment.

Цель изобретени  - уменьшение количества сточных вод и возможность одновременной очистки от газообразных примесей.The purpose of the invention is to reduce the amount of wastewater and the possibility of simultaneous purification from gaseous impurities.

Это достигаетс  способом получени  газов , содержащих водород и/или окись углерода , включаюихим неполное сжигание углеводородов , охлаждение подуктов сжигани  до температуры не ниже 200-210°С и очистку их от твердых частиц в циклоне,This is achieved by a method of producing gases containing hydrogen and / or carbon monoxide, including the incomplete combustion of hydrocarbons, cooling the combustion products to a temperature not lower than 200-210 ° C and purifying them from solid particles in a cyclone,

а затем водной промывкой, в котором водную промывку осуществл ют при температуре , равной, по меньшей мере, точке росы газа, а водную суспензию, полученную на этой стадии, дел т на два потока в объемном соотношении 1:5-20, больший из которых возвращают на стадию промывки, а меньший - на стадию охлаждени  таза.and then water washing, in which the water washing is carried out at a temperature equal to at least the dew point of the gas, and the aqueous suspension obtained at this stage is divided into two streams in a volume ratio of 1: 5-20, the largest of which return to the washing stage, and the smaller one to the pelvic cooling stage.

Claims (2)

Предлагаемый способ позвол ет свести до минимума количество сточных вод из20 за того, что при указанных услови х часть промывной воды возвращают в сырой газ. полностью испар ют и образующиес  сухие частицы золы очищают в циклоне, без образовани  суспензии золы. Кроме того, этот способ позвол ет одновременно очищать газ от примесей сернистых соединений и цианистого водорода, снижа  их содержание с 110 до 12-20 мг/м, т. е. в 10 раз. Пример. В установке нефть превращают в газ в реакторе с помощью кислорода, получаемого в потоке продукта сырого газа в количестве 3 X 10 нормальных кубических метров в день. Температура 1400°С, давление 30 бар. Сырой газ содержит 3 вес.% сажи. Газообразные примеси присутствуют в количестве 110 мг/нормальный м. Эти примеси в основном состо т из соединений серы - HjS, COS и следов HCN. Сырой газ охлаждают до 250°С в теплообменнике непр мого действи . Испаритель доводит температуру газового потока до 180°С. Циклон удал ет сажу в количестве около 90%. Оставщуюс  часть сажи удал ют в промывном аппарате. Поступающий вод ной поток после охладител  (нагревател ) имеет температуру 180°С. В состо НИИ равновеси  поток содержит 100°/п сажи, поступающей с газовым потоком. Газовый поток содержит еще газовые примеси вместе с вод ным паром, в результате получаетс  поток воды 25-210 т/день. Эта вода содержит почти все газовые примеси . Поток газа представл ет собой очищенный газовый продукт, освобожденный от сажи, с содержанием газовых примесей не более, чем 12 мг/нормальный м, поток воды очищаетс  паром в отпарной колонне . Выход щий поток воды около 210 т/день содержит не более 5 мг/кг примесей, поток газа 28-130 т/день содержит 2-20 мг/кг газообразных примесей, причем почти все примеси присутствуют в продукте сырого газа. Поток газа находитс  в контакте с сульфинолом дл  удалени  соединений серы, а оставшиес  следы HCN полностью окисл ютс  воздухом в установке дл  сжигани . Формула изобретени  Способ получени  газов, содержащих водород и/или окись углерода, включающий неполное сжигание углеводородов, охлаждение продуктов сжигани  до температуры не ниже 200-210°С и очистку их от твердых частиц в циклоне, а затем водной промывкой , отличающийс  тем, что, с целью уменьшени  количества сточных вод и одновременной очистки от газообразных примесей , водную промывку осуществл ют при температуре, равной, по меньщей мере, точке росы газа, а водную суспензию, полученную на этой стадии, дел т на два потока в объемном соотношении 1:5-20, больший из которых возвращают на стадию промывки , а меньщий - на стадию охлаждени  газа. Источники информации, прин тые во внимание при экспертизе 1.Авторское свидетельство СССР oNb 183188, кл. В 01 D 45/12, 06.12.62. The proposed method makes it possible to minimize the amount of wastewater from 20 because under these conditions, part of the wash water is returned to the raw gas. completely evaporated and the resulting dry ash particles are cleaned in a cyclone, without forming a suspension of ash. In addition, this method allows you to simultaneously purify the gas from the impurities of sulfur compounds and hydrogen cyanide, reducing their content from 110 to 12-20 mg / m, i.e., 10 times. Example. In the plant, the oil is converted into gas in a reactor using oxygen produced in the product stream of raw gas in the amount of 3 X 10 normal cubic meters per day. Temperature 1400 ° C, pressure 30 bar. Crude gas contains 3 wt.% Carbon black. Gaseous impurities are present in an amount of 110 mg / normal m. These impurities consist mainly of sulfur compounds — HjS, COS, and traces of HCN. The raw gas is cooled to 250 ° C in an indirect heat exchanger. The evaporator brings the temperature of the gas stream to 180 ° C. The cyclone removes carbon black in an amount of about 90%. The remaining soot is removed in a washer. The incoming water flow after the cooler (heater) has a temperature of 180 ° C. In the state of the scientific research institute of equilibrium, the stream contains 100 ° / n of soot entering with the gas stream. The gas stream contains more gas impurities along with water vapor, resulting in a flow of water of 25-210 tons / day. This water contains almost all gas impurities. The gas stream is a purified gas product, free from soot, with a gas impurity content of not more than 12 mg / normal m, and the water stream is cleaned with steam in a stripping column. The output water flow of about 210 tons / day contains no more than 5 mg / kg of impurities, the gas flow of 28-130 tons / day contains 2-20 mg / kg of gaseous impurities, with almost all of the impurities present in the raw gas product. The gas stream is in contact with the sulfinol to remove the sulfur compounds, and the remaining traces of HCN are completely oxidized by the air in the incinerator. Claims method for producing gases containing hydrogen and / or carbon monoxide, including incomplete combustion of hydrocarbons, cooling of the combustion products to a temperature not lower than 200-210 ° C and cleaning them from solid particles in a cyclone, and then water washing, characterized in that In order to reduce the amount of wastewater and simultaneously remove any gaseous impurities, the water washing is carried out at a temperature equal to at least the dew point of the gas, and the aqueous suspension obtained at this stage is divided into two streams 1: 5–20, the larger of which is returned to the washing stage, and the smaller one to the gas cooling stage. Sources of information taken into account during the examination 1. USSR author's certificate oNb 183188, cl. B 01 D 45/12, 06.12.62. 2.Ужов В. Н. и М гков Б. И. Очистка промыщленных газов фильтрами. 1970, с. 234-236.2. Uzhov V.N. and Mgkov B.I. Cleaning of industrial gases by filters. 1970, p. 234-236.
SU742001184A 1973-02-26 1974-02-25 Method of obtaining gases SU659071A3 (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NLAANVRAGE7302626,A NL171691C (en) 1973-02-26 1973-02-26 PROCESS FOR THE PREPARATION OF HYDROGEN AND / OR CARBON MONOXIDE-CONTAINING GASES BY INCOMPLETE BURNING OF FUELS AND SEPARATION OF THE SOLID PARTICLES THEREFORE.

Publications (1)

Publication Number Publication Date
SU659071A3 true SU659071A3 (en) 1979-04-25

Family

ID=19818305

Family Applications (1)

Application Number Title Priority Date Filing Date
SU742001184A SU659071A3 (en) 1973-02-26 1974-02-25 Method of obtaining gases

Country Status (14)

Country Link
JP (1) JPS5749078B2 (en)
BE (1) BE811058A (en)
CA (1) CA1018328A (en)
CS (1) CS192509B2 (en)
DD (1) DD110050A5 (en)
DE (1) DE2409008C2 (en)
FR (1) FR2219112B1 (en)
GB (1) GB1458448A (en)
IN (1) IN141160B (en)
IT (1) IT1008944B (en)
NL (1) NL171691C (en)
NO (1) NO137492C (en)
SE (1) SE386143B (en)
SU (1) SU659071A3 (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
NL7600481A (en) * 1976-01-19 1977-07-21 Shell Int Research PROCESS FOR SEPARATING DRY SOLIDS PARTICLES FROM A HOT GAS.
GB1544002A (en) * 1976-10-21 1979-04-11 Shell Int Research Process for the separation of dry particulate matter from a hot gas
US4219402A (en) * 1978-05-30 1980-08-26 Exxon Research & Engineering Co. Integration of stripping of fines slurry in a coking and gasification process
US4189307A (en) * 1978-06-26 1980-02-19 Texaco Development Corporation Production of clean HCN-free synthesis gas
DE2947222A1 (en) * 1979-11-23 1981-05-27 Carbon Gas Technologie GmbH, 4030 Ratingen METHOD FOR GASIFYING SOLID, DUST-MADE TO PIECE-LIKE CARBONATED MATERIAL
NL8203582A (en) * 1982-09-16 1984-04-16 Shell Int Research METHOD FOR PREPARING SYNTHESIS GAS
DE3837587C1 (en) * 1988-11-05 1990-05-23 Krupp Koppers Gmbh, 4300 Essen, De
DE4004874A1 (en) * 1990-02-16 1991-08-29 Krupp Koppers Gmbh METHOD FOR OPERATING A PLANT FOR GASIFYING SOLID FUELS
JPH04191184A (en) * 1990-11-27 1992-07-09 Honda Motor Co Ltd Method of assembling front component of vehicle body
DE10049227B4 (en) * 2000-09-28 2007-02-01 Bu Bioenergie & Umwelttechnik Ag Procedures for gas purification of process gas from gasification processes

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AT205010B (en) * 1956-08-10 1959-08-25 Bataafsche Petroleum Method of simultaneous cooling and cleaning of hot gases
FR1217355A (en) * 1957-12-31 1960-05-03 Bataafsche Petroleum Process for removing soot from gases

Also Published As

Publication number Publication date
CA1018328A (en) 1977-10-04
NL171691B (en) 1982-12-01
AU6595874A (en) 1975-08-28
SE386143B (en) 1976-08-02
NL7302626A (en) 1974-08-28
JPS5749078B2 (en) 1982-10-20
NO137492B (en) 1977-11-28
DE2409008C2 (en) 1985-05-30
NO137492C (en) 1978-03-08
JPS49118702A (en) 1974-11-13
NO740633L (en) 1974-08-27
CS192509B2 (en) 1979-08-31
NL171691C (en) 1983-05-02
IT1008944B (en) 1976-11-30
DE2409008A1 (en) 1974-08-29
BE811058A (en) 1974-08-16
GB1458448A (en) 1976-12-15
FR2219112A1 (en) 1974-09-20
FR2219112B1 (en) 1977-06-10
DD110050A5 (en) 1974-12-05
IN141160B (en) 1977-01-29

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