US1646349A - Thermal decomposition of hydrocarbons - Google Patents

Thermal decomposition of hydrocarbons Download PDF

Info

Publication number
US1646349A
US1646349A US79896A US7989626A US1646349A US 1646349 A US1646349 A US 1646349A US 79896 A US79896 A US 79896A US 7989626 A US7989626 A US 7989626A US 1646349 A US1646349 A US 1646349A
Authority
US
United States
Prior art keywords
iron
hydrocarbons
tubes
thermal decomposition
chrome
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.)
Expired - Lifetime
Application number
US79896A
Inventor
Jr George O Curme
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.)
Carbide and Carbon Chemicals Corp
Original Assignee
Carbide and Carbon Chemicals Corp
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 Carbide and Carbon Chemicals Corp filed Critical Carbide and Carbon Chemicals Corp
Priority to US79896A priority Critical patent/US1646349A/en
Application granted granted Critical
Publication of US1646349A publication Critical patent/US1646349A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J19/00Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J19/0006Controlling or regulating processes
    • B01J19/002Avoiding undesirable reactions or side-effects, e.g. avoiding explosions, or improving the yield by suppressing side-reactions
    • B01J19/0026Avoiding carbon deposits
    • 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
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S585/00Chemistry of hydrocarbon compounds
    • Y10S585/949Miscellaneous considerations
    • Y10S585/95Prevention or removal of corrosion or solid deposits

Definitions

  • This invention comprises a process for thermally decomposing hydrocarbons.
  • hydrocarbons in general are decomposed at sufliciently elevated temperatures, and that the decomposition can be so regulated that it produces hydrocarbons of smaller molecular weight than the hydrocarbons treated. Under these conditions a considerable proportion of chemically unsaturated hydrocarbons, such as the olefines, is normally present in the decomposition product.
  • chrome-iron was substituted for iron as the material of the jacket. This alloy was found to resist corrosion very much better than iron, but a more important 'and entirely unexpected advantage of m Drawingv Application filed January 7, 1926.
  • Serial-No. vassaflElssuE chrome-iron was soon discovered. It was foundthat when the copper lining of a chrome-iron tube became perforated and the hydrocarbon gases came into contact with the Jacket, there was little or no deposition of carbon on the portion of the 'acket thus exposed, and no detrimental e ect on the yield of olefine hydrocarbons. Under similar conditions with iron jackets the tube would become blocked me very short time by carbon built up on the exposed iron.
  • the chrome-iron preferably contains upward of 20% of chromium, but the invention is not restricted to such percentages as a smaller proportion gives a useful effect, especially at lower operatingtemperatures.
  • the best results obtained so far have been with material containing 26 to 29% chromlum.
  • the tubes are preferably composed of a workable alloy, such as is described in the patent to Becket and McQuigg 1,454,464 dated May 8, 1923.
  • Seamless drawn tubing is preferred but tubes fabricated from sheet by fusion welding maybe used.
  • the weld should be made with an alloy of approximately the same composition as the sheet forming the body of the tube. Even when this practice is followed a small amount of carbon may deposit on the weld when the tube 1s in use,-presumably because the composition of the weld is somewhat changed in the welding operation, as by oxidation of chromium. Carbon also accumulates slowly on the walls of any tube carrying heated hydrocarbon vapors in the temperature range above mentioned presumably from the baking of heavy tars formed as by-products in the cracking reaction which condense out at the temperature of operation.
  • This carbon is readily removed by periodically passing air through the tube while heating it to a sufiicient temlperature to bring about oxidation of the cargiving exce lent '
  • the invention is especially valuable p to temperatures in the vicinity 0f1900 C.', it is applicable to many processes where the temperatures and products are quite dif-- ferent.
  • the ability of chrome-iron to resist oxidation at high temperatures is known, and the inventio'n'resides in the use of the alloy in contact with hydrocarbon material under such conditions that carbon deposition would preclude the use of commercialiron. It is intended to cover all such uses of chrome-iron in the appended claims.
  • the rocess which comprises thermally decompos ng hydrocarbons while the latter are in contact with an alloy consisting predominantly of'chromium and iron and con i I and chromium tainin'g at least 20% such conditions that contact of commercial iron with the decomposing hydrocarbon would give rise to seriously interfering deposition of carbon.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Description

Patented Oct. 18, 1927.
UNITED STATES PATENT .OFFICE."
GEORGE O. GURME, JR., 0! CHARLESTON, WEST VIRGINIA; ASSIGNOR TO CARBIDE AND CARBON CHEMICALS CORPORATION, A CORPORATION OF-NEW YORK. v
THERMAL DECOMPOSITION OF HYDROOARBONS.
This invention comprises a process for thermally decomposing hydrocarbons.
It is well known that hydrocarbons in general are decomposed at sufliciently elevated temperatures, and that the decomposition can be so regulated that it produces hydrocarbons of smaller molecular weight than the hydrocarbons treated. Under these conditions a considerable proportion of chemically unsaturated hydrocarbons, such as the olefines, is normally present in the decomposition product.
In an extensive-experience with processes involving the controlled-thermal decomposition of hydrocarbons, such as the process described in Patent 1,460,545 granted on July 3, 1923, to Pierre 1*). Haynes and the present applicant, various materials have been in vestigated to determine their fitness for making tubes in which to confine hydrocarbons while heating them by roducts of'combustion to temperatures as high as 1000 0. Because of its fairly good strength and resistance to oxidation at the temperatures in volved, but principally because of its cheap ness, iron was the material first chosen for the part-of the tubes which comes into contact with the combustion gases.
It was found, however, that iron exerts at 'such temperatures a powerful catalytic action on hydrocarbon vapors, promoting a reaction producing solid carbon, and the latter builds up on the walls of the tubes and soon clogs them. It was therefore necessar to line the iron tubes with copper tubing. ime no iron or copper tubing obtainable at prices permitting its industrial use for such a purpose %)as a sufliciently close approximation to a rue cylindrical surface to permit the iron tube and its copper lining accurately to interfit, a gas layer of variable thickness was present between the two tubes and interfered seriously with the heat'transfer. Furthermore the iron tubes burned out rather quickly and perforation of either the iron or the co per disabled the unit. Replacement of tu es with the attendant interference with the operation of the furnace proved to be troublesiime and expensive.
In an attempt to improve the lined tubes described above, chrome-iron was substituted for iron as the material of the jacket. This alloy was found to resist corrosion very much better than iron, but a more important 'and entirely unexpected advantage of m Drawingv Application filed January 7, 1926. Serial-No. vassaflElssuE chrome-iron was soon discovered. It was foundthat when the copper lining of a chrome-iron tube became perforated and the hydrocarbon gases came into contact with the Jacket, there was little or no deposition of carbon on the portion of the 'acket thus exposed, and no detrimental e ect on the yield of olefine hydrocarbons. Under similar conditions with iron jackets the tube would become blocked me very short time by carbon built up on the exposed iron.
Accordingly, it was indicated that unlined chrome-iron tubes could be substituted for copper-lined iron tubes with great advantage, and the unlined tubes have one into extensive useand are results. i
For use at the temperatures discussed above, the chrome-iron preferably contains upward of 20% of chromium, but the invention is not restricted to such percentages as a smaller proportion gives a useful effect, especially at lower operatingtemperatures. The best results obtained so far have been with material containing 26 to 29% chromlum. The tubes are preferably composed of a workable alloy, such as is described in the patent to Becket and McQuigg 1,454,464 dated May 8, 1923.
Seamless drawn tubing is preferred but tubes fabricated from sheet by fusion welding maybe used. The weld should be made with an alloy of approximately the same composition as the sheet forming the body of the tube. Even when this practice is followed a small amount of carbon may deposit on the weld when the tube 1s in use,-presumably because the composition of the weld is somewhat changed in the welding operation, as by oxidation of chromium. Carbon also accumulates slowly on the walls of any tube carrying heated hydrocarbon vapors in the temperature range above mentioned presumably from the baking of heavy tars formed as by-products in the cracking reaction which condense out at the temperature of operation. This carbon is readily removed by periodically passing air through the tube while heating it to a sufiicient temlperature to bring about oxidation of the cargiving exce lent 'While the invention is especially valuable p to temperatures in the vicinity 0f1900 C.', it is applicable to many processes where the temperatures and products are quite dif-- ferent. The ability of chrome-iron to resist oxidation at high temperatures is known, and the inventio'n'resides in the use of the alloy in contact with hydrocarbon material under such conditions that carbon deposition would preclude the use of commercialiron. It is intended to cover all such uses of chrome-iron in the appended claims.
I claim:
1. The process which comprises thermally decomposing hydrocarbons while the latter are in contact with an alloy consisting predominantly of chromium and'iron.
2. The process which comprises thermally decomposing hydrocarbons while the latter are in contact with, an alloy consisting predominantly of chromium and iron under 'such conditions that contact of commercial iron with the decomposing hydrocarbon would give rise toseriously interfering deposition ofcarbon. V
3. The rocess which comprises thermally decompos ng hydrocarbons while the latter are in contact with an alloy consisting predominantly of'chromium and iron and con i I and chromium tainin'g at least 20% such conditions that contact of commercial iron with the decomposing hydrocarbon would give rise to seriously interfering deposition of carbon. a
4. The process which comprises thermally decomposing hydrocarbons by confining the same at least in part. of'an alloy consisting predominantly of iron and, applying combustion gases tosaid wall to heat the hydrocarbons.
5. The process which comprises thermallyv decomposing hydrocarbons by confining the same at least in partby a wall constructed of chrome-iron contalnlng at least 20% of chromium, and applying combustion gases ,to said wall to heat the hydrocarbons; v
6. The process of thermally decomposing hydrocarbons which comprises confining the same in a chrome-iron tube resistant to oxidation at temperatures as high as 900 C., and hea ing the exterior of the tube to about said temperature by contact of combustion gases therewith.
In testimony whereof, I aflix my signature. I
GEORGE o. CURMEQJR.
by a wall constructed of chromium under 1
US79896A 1926-01-07 1926-01-07 Thermal decomposition of hydrocarbons Expired - Lifetime US1646349A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US79896A US1646349A (en) 1926-01-07 1926-01-07 Thermal decomposition of hydrocarbons

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US79896A US1646349A (en) 1926-01-07 1926-01-07 Thermal decomposition of hydrocarbons

Publications (1)

Publication Number Publication Date
US1646349A true US1646349A (en) 1927-10-18

Family

ID=22153490

Family Applications (1)

Application Number Title Priority Date Filing Date
US79896A Expired - Lifetime US1646349A (en) 1926-01-07 1926-01-07 Thermal decomposition of hydrocarbons

Country Status (1)

Country Link
US (1) US1646349A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2537079A (en) * 1948-06-04 1951-01-09 Standard Oil Dev Co Prevention of coke formation in pyrolysis of acetone
DE756064C (en) * 1935-11-09 1953-11-09 Ig Farbenindustrie Ag Devices made of high-alloy chromium steel containing silicon for the thermal treatment of coal and hydrocarbons

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE756064C (en) * 1935-11-09 1953-11-09 Ig Farbenindustrie Ag Devices made of high-alloy chromium steel containing silicon for the thermal treatment of coal and hydrocarbons
US2537079A (en) * 1948-06-04 1951-01-09 Standard Oil Dev Co Prevention of coke formation in pyrolysis of acetone

Similar Documents

Publication Publication Date Title
US2063596A (en) Thermal treatment of carbon compounds
US2904502A (en) Method of cracking hydrocarbons
US1646349A (en) Thermal decomposition of hydrocarbons
US2393778A (en) Process and apparatus for the pyrolysis of organic compounds
US1925784A (en) Process for making diphenyl
US1296367A (en) Process and apparatus for cracking and distilling hydrocarbons.
GB411477A (en) Improvements in the manufacture and production of liquid hydrocarbons of low boiling point by the thermal treatment of tars, mineral oils and the like
US1988873A (en) Thermal treatment of hydrocarbons
US1868127A (en) Production of valuable hydrocarbons
USRE18148E (en) Qboboe q
US2034292A (en) Production of carbon chlorides
US3234300A (en) Production of acetylene by the partial combustion process
US2403735A (en) Hydrogen chloride manufacture
JPS6317117B2 (en)
US2271955A (en) Method and apparatus for prevention of formations in transfer lines
US1983415A (en) Process of thermally decomposing hydrocarbons
US1819732A (en) Process for the production of hydrogen and carbon from hydrocarbons
US1938609A (en) Production of diphenyl from benzene
US1835426A (en) Destructive hydrogenation of carbonaceous materials
US1430585A (en) Process of producing aromatic hydrocarbons
US2060356A (en) Production of unsaturated hydrocarbons
US1894764A (en) Production of carbon black
US3455659A (en) Superheating ammonia
US2537079A (en) Prevention of coke formation in pyrolysis of acetone
Holmen et al. Coke formation on nickel-chromium-iron alloys