[go: up one dir, main page]

WO1986006055A1 - Partial combustion of hydrocarbons - Google Patents

Partial combustion of hydrocarbons Download PDF

Info

Publication number
WO1986006055A1
WO1986006055A1 PCT/GB1986/000198 GB8600198W WO8606055A1 WO 1986006055 A1 WO1986006055 A1 WO 1986006055A1 GB 8600198 W GB8600198 W GB 8600198W WO 8606055 A1 WO8606055 A1 WO 8606055A1
Authority
WO
WIPO (PCT)
Prior art keywords
process according
cone
fuel
containing gas
oxygen containing
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.)
Ceased
Application number
PCT/GB1986/000198
Other languages
French (fr)
Inventor
Denis Henry Desty
David Montagu Whitehead
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.)
BP PLC
Original Assignee
BP PLC
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 BP PLC filed Critical BP PLC
Priority to GB08628851A priority Critical patent/GB2185038A/en
Priority to NL8620131A priority patent/NL8620131A/en
Publication of WO1986006055A1 publication Critical patent/WO1986006055A1/en
Priority to NO864711A priority patent/NO864711D0/en
Anticipated expiration legal-status Critical
Ceased legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C01—INORGANIC CHEMISTRY
    • C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B3/00—Hydrogen; Gaseous mixtures containing hydrogen; Separation of hydrogen from mixtures containing it; Purification of hydrogen
    • C01B3/02—Production of hydrogen or of gaseous mixtures containing a substantial proportion of hydrogen
    • C01B3/32—Production 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
    • C01B3/34—Production 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
    • C01B3/36—Production 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
    • C01B3/363—Production 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

Definitions

  • the present invention relates to a process for the partial combustion of hydrocarbons to produce useful products.
  • the present invention relates to a conversion process for such a purpose and which is flexible in operation.
  • a process for the conversion of hydrocarbons comprising the steps of (a) passing a gaseous fuel or an oxygen containing gas through a foraminous cone so as to mix with oxygen containing gas or a gaseous fuel issuing from a nozzle located at the throat of the cone, (b) the fuel/oxygen containing gas composition being fuel rich, (c) igniting and reacting the . resultant mixture, and (d) withdrawing the products of the process.
  • the fuel is suitably natural gas, liquid petroleum g-_3, residual fuels, liquid containing dispersed solid fuels etc. and the oxygen containing gas may be pure oxygen, oxygen-enriched air or air.
  • the reactants are preferably pre-heated before introduction to the reactor.
  • the reactor for the process has an external housing which encloses the foraminous cone *
  • the housing may have holes located downstream of the cone in order to allow quenching e.g. by the use of radially injected water, of the products to conserve any higher hydrocarbons. Also the products may be quenched with gaseous or liquid hydrocarbons to increase the yields of higher hydrocarbons. Thus the quenching stage may be used to control the final products of the claimed process.
  • the materials of construction of the reactor include metals, such as stainless steel, and ceramics and are chosen to withstand the temperature and conditions of reactor operation.
  • the foraminous cone is preferably a cone having rows of holes extending along radial lines from the throat of the cone.
  • the rows may be straight or have a curved configuration.
  • the cross-section of the holes may increase from the throat to the mouth of the cone.
  • the hole size is dependent on the required throughput and pressure drop of the reactor (the pressure drop usually being of the order 2-3 ⁇ Z of the pressure in the system).
  • the holes may be of various shapes such as circular, square, diamond-like, oval etc.
  • the nozzle preferably has a plurality of outlets, each outlet preferably being adapted to direct fuel or oxygen containing gas between the rows of holes, most preferably one outlet being associated with a specific row of holes.
  • the nozzle may be cooled e.g. by a steam or water line.
  • a reactor arrangement which may be adapted for use in the present invention is disclosed in UK patent application No 1575641.
  • the preferred fuel rich composition is 1.1 to 5 times the ratio of fuel/oxygen for complete combustion to carbon dioxide and water (stoichiometric ratio), but these limits are extendable if operation at system pressures of greater than atmospheric are envisaged.
  • the composition will vary dependent upon the fuel used. Commercial reactor systems would probably be operated at elevated pressures of up to 100 bar. It is also envisaged that hydrogen or steam may be co-fed with either the hydrocarbon fuel or the oxygen containing gas or both.
  • the products of the reaction vary depending upon the reactants, conditions, quenching etc. and may include carbon monoxide, hydrogen, water, carbon dioxide, methane and higher hydrocarbons. It is envisaged that for the conversion of large quantities of fuel, an array of reactors could be used.
  • the reactor takes the form of cylindrical housing 1 which encloses a foraminous cone 2.
  • a nozzle is located at the throat of the cone 2 for supplying either oxygen or fuel to the interior of the cone.
  • the nozzle is supplied by tube 3 which has its longitudinal axis co-axial with the axis of the housing.
  • oxygen is supplied from feed pipes (not shown) into the annular space 5 between the housing 4 and the tube 3 and passes through the holes 9.
  • An intermediate tube (not shown) is connected to a source of water or steam which acts as a coolant for the nozzle 3.
  • the tube 3 is connected to a fuel supply (not shown) and the fuel emerges from outlets 6 in the nozzle.
  • the cone 2 which may be fabricated from say stainless steel, ceramic materials, or quartz has rows of holes 9 extending along radial lines from the throat of the cone. The rows have a slightly curved configuration and the cross-section of the holes increases in size from the throat to the mouth of the cone. In the present example the diameter of the holes was in the range 2 to 3 mm ( Figure 2).
  • the nozzle has a plurality of outlets capable of directing fuel along the internal surface of the cone.
  • the nozzle outlets are adapted to direct the fuel between the rows of holes, each outlet being associated with one row of holes.
  • the reactor may be used either (a) with fuel gas emerging from the nozzle outlets so as to mix with oxygen or an oxygen containing gas passing through the holes of the cone or alternatively (b) with oxygen or an oxygen containing gas emerging from the nozzle outlets so as to mix with fuel passing through the holes of the cone.
  • the present example is directed towards alternative (a).
  • fuel gas in the form of methane is supplied to the tube 3 and emerges in a series of jets from the nozzle outlets.
  • Oxygen or oxygen-enriched air is supplied from the plenum chamber (not shown) and emerges from outlets into the annular space 5 and thereby passes through the holes into the interior of the cone.
  • the angle of the methane and oxygen jets intimately mixes the methane and oxygen.
  • the methane/oxygen mixture is ignited within the cone by means of a spark igniter 8.
  • the products of the reaction are drawn off downstream from the cone.
  • Further holes 7 in the housing may be used to pass quenching steam or water into the reaction zone.
  • Figure 2 shows the cone 2 in greater detail.
  • the ten datum lines 20 are equi-spaced at 36° intervals * For example, relative to each datum line is a row of four holes, there being a total of forty holes in the cone.
  • the cross section of the hole increases in the direction from the throat to the mouth of the cone.
  • Figure 2(a) is a view from the inside of the cone and figure 2(b) is a side view.
  • the table shows results obtained for the conversion process using natural gas as fuel and oxygen or oxygen enriched air as the oxygen containing gas. There was no pre-heatlng of the reactant gases and there was little or no soot formation.
  • Run numbers 1 to 4 show the effect of increasing oxygen content of the reactant gases
  • run numbers 5 to 10 show the production of C2+ in the products.
  • the relative yields of C2+, carbon monoxide and hydrogen in the product gases may be controlled. Further flexibility of control may be achieved by suitable application of a quenching step (run numbers 5 to 12 are the subject of water quenching) to give enhanced yields of C2+ *

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • General Health & Medical Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Combustion & Propulsion (AREA)
  • Inorganic Chemistry (AREA)
  • Hydrogen, Water And Hydrids (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

A process for the conversion of hydrocarbons in which a gaseous fuel is mixed with an oxygen containing gas in a reactor (1) by passing one component through an annular space (5) and then through the holes (9) of a foraminous cone (2) and the other component through the nozzle (3) located at the throat of the cone. The resultant fuel/oxygen containing gas composition is fuel rich and is ignited (B) and reacted in the reaction chamber. The product of the process may be withdrawn and collected.

Description

Partial combustion of hydrocarbons
The present invention relates to a process for the partial combustion of hydrocarbons to produce useful products.
It is desirable to convert readily available feedstocks such as natural gas into more commercially useful products such as higher hydrocarbons, unsaturated hydrocarbons, synthesis gas, and methanol. The present invention relates to a conversion process for such a purpose and which is flexible in operation.
Thus according to the present invention there is provided a process for the conversion of hydrocarbons comprising the steps of (a) passing a gaseous fuel or an oxygen containing gas through a foraminous cone so as to mix with oxygen containing gas or a gaseous fuel issuing from a nozzle located at the throat of the cone, (b) the fuel/oxygen containing gas composition being fuel rich, (c) igniting and reacting the. resultant mixture, and (d) withdrawing the products of the process.
The fuel is suitably natural gas, liquid petroleum g-_3, residual fuels, liquid containing dispersed solid fuels etc. and the oxygen containing gas may be pure oxygen, oxygen-enriched air or air. The reactants are preferably pre-heated before introduction to the reactor.
The reactor for the process has an external housing which encloses the foraminous cone* The housing may have holes located downstream of the cone in order to allow quenching e.g. by the use of radially injected water, of the products to conserve any higher hydrocarbons. Also the products may be quenched with gaseous or liquid hydrocarbons to increase the yields of higher hydrocarbons. Thus the quenching stage may be used to control the final products of the claimed process.
The materials of construction of the reactor include metals, such as stainless steel, and ceramics and are chosen to withstand the temperature and conditions of reactor operation.
The foraminous cone is preferably a cone having rows of holes extending along radial lines from the throat of the cone. The rows may be straight or have a curved configuration. The cross-section of the holes may increase from the throat to the mouth of the cone. The hole size is dependent on the required throughput and pressure drop of the reactor (the pressure drop usually being of the order 2-3^Z of the pressure in the system). The holes may be of various shapes such as circular, square, diamond-like, oval etc. The nozzle preferably has a plurality of outlets, each outlet preferably being adapted to direct fuel or oxygen containing gas between the rows of holes, most preferably one outlet being associated with a specific row of holes. The nozzle may be cooled e.g. by a steam or water line. A reactor arrangement which may be adapted for use in the present invention is disclosed in UK patent application No 1575641.
At atmospheric pressure the preferred fuel rich composition is 1.1 to 5 times the ratio of fuel/oxygen for complete combustion to carbon dioxide and water (stoichiometric ratio), but these limits are extendable if operation at system pressures of greater than atmospheric are envisaged. The composition will vary dependent upon the fuel used. Commercial reactor systems would probably be operated at elevated pressures of up to 100 bar. It is also envisaged that hydrogen or steam may be co-fed with either the hydrocarbon fuel or the oxygen containing gas or both.
The products of the reaction vary depending upon the reactants, conditions, quenching etc. and may include carbon monoxide, hydrogen, water, carbon dioxide, methane and higher hydrocarbons. It is envisaged that for the conversion of large quantities of fuel, an array of reactors could be used.
The invention will now be described by way of example only and with reference to Figures 1 and 2 of the accompanying drawings. The reactor takes the form of cylindrical housing 1 which encloses a foraminous cone 2. A nozzle is located at the throat of the cone 2 for supplying either oxygen or fuel to the interior of the cone. The nozzle is supplied by tube 3 which has its longitudinal axis co-axial with the axis of the housing.
In the present example, oxygen is supplied from feed pipes (not shown) into the annular space 5 between the housing 4 and the tube 3 and passes through the holes 9. An intermediate tube (not shown) is connected to a source of water or steam which acts as a coolant for the nozzle 3. The tube 3 is connected to a fuel supply (not shown) and the fuel emerges from outlets 6 in the nozzle. The cone 2 which may be fabricated from say stainless steel, ceramic materials, or quartz has rows of holes 9 extending along radial lines from the throat of the cone. The rows have a slightly curved configuration and the cross-section of the holes increases in size from the throat to the mouth of the cone. In the present example the diameter of the holes was in the range 2 to 3 mm (Figure 2).
The nozzle has a plurality of outlets capable of directing fuel along the internal surface of the cone. The nozzle outlets are adapted to direct the fuel between the rows of holes, each outlet being associated with one row of holes.
The reactor may be used either (a) with fuel gas emerging from the nozzle outlets so as to mix with oxygen or an oxygen containing gas passing through the holes of the cone or alternatively (b) with oxygen or an oxygen containing gas emerging from the nozzle outlets so as to mix with fuel passing through the holes of the cone. The present example is directed towards alternative (a).
During use of the reactor, fuel gas in the form of methane is supplied to the tube 3 and emerges in a series of jets from the nozzle outlets. Oxygen or oxygen-enriched air is supplied from the plenum chamber (not shown) and emerges from outlets into the annular space 5 and thereby passes through the holes into the interior of the cone. The angle of the methane and oxygen jets intimately mixes the methane and oxygen. The methane/oxygen mixture is ignited within the cone by means of a spark igniter 8. The products of the reaction are drawn off downstream from the cone.
Further holes 7 in the housing may be used to pass quenching steam or water into the reaction zone.
Figure 2 shows the cone 2 in greater detail. The ten datum lines 20 are equi-spaced at 36° intervals* For example, relative to each datum line is a row of four holes, there being a total of forty holes in the cone. The cross section of the hole increases in the direction from the throat to the mouth of the cone. Figure 2(a) is a view from the inside of the cone and figure 2(b) is a side view. The table shows results obtained for the conversion process using natural gas as fuel and oxygen or oxygen enriched air as the oxygen containing gas. There was no pre-heatlng of the reactant gases and there was little or no soot formation.
Run numbers 1 to 4 show the effect of increasing oxygen content of the reactant gases, and run numbers 5 to 10 show the production of C2+ in the products. By variation of the oxygen content of the reactant gases, the relative yields of C2+, carbon monoxide and hydrogen in the product gases may be controlled. Further flexibility of control may be achieved by suitable application of a quenching step (run numbers 5 to 12 are the subject of water quenching) to give enhanced yields of C2+*
Table
Figure imgf000007_0001

Claims

Claims:
1 A process for the conversion of hydrocarbons comprising the steps of (a) passing a gaseous fuel or an oxygen containing gas through a foraminous cone so as to mix with oxygen containing gas or a gaseous fuel issuing from a nozzle located at the throat of the cone, (b) the fuel/oxygen containing gas composition being fuel rich, (c) igniting and reacting the resultant mixture, and (d) withdrawing the products of the process.
2 A process according to claim 1 in which the gaseous fuel is natural gas or methane. 3 A process according to claim 1 or claim 2 in which the oxygen containing gas is pure oxygen, oxygen-enriched air or air. 4 A process according to any of claims 1 to 3 in which the cone has rows of holes extending along radial lines from the throat of the cone. 5 A process according to claim 4 in which the rows are straight or have a curved configuration. 6 A process according to claim 4 or claim 5 in which the cross-section of the holes increases from the throat to the mouth of the cone. 7 A process according to any of the preceding claims in which the nozzle has a plurality of outlets. 8 A process according to claim 7 in which each outlet is adapted to direct the fuel or the oxygen containing gas between the rows of holes of the cone. 9 A process according to claim 8 in which each outlet is associated with a specific row of holes.
10 A process according to any of the preceding claims in which the products of the reaction are quenched prior to withdrawal. 11 A process according to any of the preceding claims in which hydrogen or steam is co-fed with the fuel or the oxygen containing gas or both. 12 A process according to any of the preceding claims which is operated at elevated pressure. 13 A process according to any of the preceding claims in which one or both of the gaseous fuel and oxygen containing gas are pre-heated prior to ignition and reaction.
PCT/GB1986/000198 1985-04-11 1986-04-11 Partial combustion of hydrocarbons Ceased WO1986006055A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
GB08628851A GB2185038A (en) 1985-04-11 1986-04-11 Partial combustion of hydrocarbons
NL8620131A NL8620131A (en) 1985-04-11 1986-04-11 PARTIAL COMBUSTION OF HYDROCARBONS.
NO864711A NO864711D0 (en) 1985-04-11 1986-11-25 PARTIAL COMBUSTION OF HYDROCARBONES.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
GB8509271 1985-04-11
GB858509271A GB8509271D0 (en) 1985-04-11 1985-04-11 Conversion process

Publications (1)

Publication Number Publication Date
WO1986006055A1 true WO1986006055A1 (en) 1986-10-23

Family

ID=10577454

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/GB1986/000198 Ceased WO1986006055A1 (en) 1985-04-11 1986-04-11 Partial combustion of hydrocarbons

Country Status (10)

Country Link
JP (1) JPS62502962A (en)
AU (1) AU582240B2 (en)
BE (1) BE904585A (en)
CA (1) CA1265164A (en)
DE (1) DE3690190T1 (en)
FR (1) FR2589848A1 (en)
GB (2) GB8509271D0 (en)
IT (1) IT1221029B (en)
NL (1) NL8620131A (en)
WO (1) WO1986006055A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2119888C1 (en) * 1998-02-10 1998-10-10 Тк Сибур Нн Method of producing synthesis gas

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1843063A (en) * 1932-01-26 Of cabbon monoxide anj
US2638452A (en) * 1953-05-12 Process fob making synthesis gas
US2701756A (en) * 1955-02-08 Manufacture of synthesis gas
GB827719A (en) * 1955-02-05 1960-02-10 Reginald Percy Frazer Improvements relating to the thermal decomposition of hydrocarbons
GB827720A (en) * 1955-02-05 1960-02-10 Reginald Percy Fraser Improvements relating to the thermal decomposition of hydrocarbons

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1575641A (en) * 1977-02-23 1980-09-24 Secr Defence Combustion apparatus

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1843063A (en) * 1932-01-26 Of cabbon monoxide anj
US2638452A (en) * 1953-05-12 Process fob making synthesis gas
US2701756A (en) * 1955-02-08 Manufacture of synthesis gas
GB827719A (en) * 1955-02-05 1960-02-10 Reginald Percy Frazer Improvements relating to the thermal decomposition of hydrocarbons
GB827720A (en) * 1955-02-05 1960-02-10 Reginald Percy Fraser Improvements relating to the thermal decomposition of hydrocarbons

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
RU2119888C1 (en) * 1998-02-10 1998-10-10 Тк Сибур Нн Method of producing synthesis gas

Also Published As

Publication number Publication date
GB2185038A (en) 1987-07-08
GB8628851D0 (en) 1987-01-07
BE904585A (en) 1986-10-13
NL8620131A (en) 1987-02-02
IT1221029B (en) 1990-06-21
JPS62502962A (en) 1987-11-26
CA1265164A (en) 1990-01-30
FR2589848A1 (en) 1987-05-15
IT8620069A0 (en) 1986-04-11
AU5776586A (en) 1986-11-05
GB8509271D0 (en) 1985-05-15
AU582240B2 (en) 1989-03-16
DE3690190T1 (en) 1987-04-23

Similar Documents

Publication Publication Date Title
SU1766282A3 (en) Method of incomplete oxidation of hydrocarbon fuel
AU604956B2 (en) Gas mixer and distributor for reactor
US4726913A (en) Conversion process
US5549877A (en) Device and process for manufacturing synthesis gases through combustion and its application
US4758375A (en) Conversion process
CN1183376A (en) Steam reforming process
PL350136A1 (en) Secondary reforming process and burner
US4775314A (en) Coal gasification burner
AU582240B2 (en) Partial combustion of hydrocarbons
GB2159153A (en) Process for the production of oxygenated hydrocarbons
EP3917874B1 (en) A process for partial oxidation
US3843307A (en) Process for incomplete combustion of hydrocarbons
GB1355541A (en) Carbon black process and apparatus
EP1307281B1 (en) Flow distributor
RU2087185C1 (en) Reactor for producing acetylene from hydrocarbons
NO864711L (en) PARTIAL COMBUSTION OF HYDROCARBONES.
SU1547843A2 (en) Reactor for thermal conversion of hydrocarbon gas
SU319233A1 (en) Reactor for producing carbon black
KR900018300A (en) Carbon black manufacturing process and device
EP0287380A2 (en) Burner for conversion process
GB1165440A (en) Process and Apparatus for the Preparation of Gases containing Hydrogen and Carbon Monoxide
EP0372658B1 (en) Partial oxidation method
SU729221A1 (en) Method of producing highly structured carbon black
RU2021124843A (en) PARTIAL OXIDATION METHOD
GB1469952A (en) Apparatus for the manufacture of gases by incomplete com bustion of a gaseous or finely-divided atomised fuel

Legal Events

Date Code Title Description
AK Designated states

Kind code of ref document: A1

Designated state(s): AU DE GB JP NL NO US

RET De translation (de og part 6b)

Ref document number: 3690190

Country of ref document: DE

Date of ref document: 19870423

WWE Wipo information: entry into national phase

Ref document number: 3690190

Country of ref document: DE