GB487983A - Method and apparatus for destructive distillation at low temperature - Google Patents

Method and apparatus for destructive distillation at low temperature

Info

Publication number
GB487983A
GB487983A GB1930137A GB1930137A GB487983A GB 487983 A GB487983 A GB 487983A GB 1930137 A GB1930137 A GB 1930137A GB 1930137 A GB1930137 A GB 1930137A GB 487983 A GB487983 A GB 487983A
Authority
GB
United Kingdom
Prior art keywords
chamber
gases
distilling
hot
condenser
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
Application number
GB1930137A
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.)
Societe Chimique de la Grande Paroisse Azote et Produits Chimiques
Original Assignee
Societe Chimique de la Grande Paroisse Azote et Produits Chimiques
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 Societe Chimique de la Grande Paroisse Azote et Produits Chimiques filed Critical Societe Chimique de la Grande Paroisse Azote et Produits Chimiques
Priority to GB1930137A priority Critical patent/GB487983A/en
Priority to NL88505A priority patent/NL50752C/xx
Priority to FR839892D priority patent/FR839892A/en
Publication of GB487983A publication Critical patent/GB487983A/en
Expired legal-status Critical Current

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B1/00—Retorts
    • C10B1/02—Stationary retorts
    • C10B1/04—Vertical retorts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B49/00—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated
    • C10B49/02—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge
    • C10B49/04—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated
    • C10B49/06—Destructive distillation of solid carbonaceous materials by direct heating with heat-carrying agents including the partial combustion of the solid material to be treated with hot gases or vapours, e.g. hot gases obtained by partial combustion of the charge while moving the solid material to be treated according to the moving bed type
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/02—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by distillation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Wood Science & Technology (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)

Abstract

487,983. Distilling and gasefying solid carbonaceous materials. ROWLEY, H. E. G. (Soc. Chimique de la Grande Paroisse- Azote & Produits Chimiques) July 12, J937, No. 19301. [Class 55 (i)] In the production of oils by low temperature distillation of coal, lignite, oil shale, petroliferous sandstone, &c. in a distillation chamber through which the material passes vertically downwards, by means of hot gases or superheated steam flowing: horizontally therethrough in a closed circuit, followed by combustion of the distilled material by means of oxygen-containing gas, the hot residue is utilized to preheat the hot gases or steam used in the distillation chamber. Superimposed chambers of a retort comprise a preheating or drying chamber A, a distilling chamber B, a combustion chamber C and a residue cooling chamber D and are utilized in combination with a condenser L and a heat exchanger E. The distilling medium is superheated by passage through the hot residue in D and then through the heat exchanger E before entering the distilling chamber B from which the gases and volatile products pass into the condenser L. Oils are recovered in the latter and the non-condensible gas or lowpressure steam, which may be compressed by a compressor M, is returned to the cycle. Hot water separated in the condenser may be utilized for the production of steam required in the process. Oxygen-containing gas is supplied to the combustion chamber C through a supply pipe 7, part of the issuing gases being used in the heat exchanger and part, after utilization in an external apparatus, such as a boiler K, being used in the preheating chamber A. The flow of gases through the chambers A and D may be horizontal or vertical.
GB1930137A 1937-07-12 1937-07-12 Method and apparatus for destructive distillation at low temperature Expired GB487983A (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
GB1930137A GB487983A (en) 1937-07-12 1937-07-12 Method and apparatus for destructive distillation at low temperature
NL88505A NL50752C (en) 1937-07-12 1938-06-23
FR839892D FR839892A (en) 1937-07-12 1938-06-27 Improvements to low temperature distillation processes and devices

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1930137A GB487983A (en) 1937-07-12 1937-07-12 Method and apparatus for destructive distillation at low temperature

Publications (1)

Publication Number Publication Date
GB487983A true GB487983A (en) 1938-06-29

Family

ID=10127114

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1930137A Expired GB487983A (en) 1937-07-12 1937-07-12 Method and apparatus for destructive distillation at low temperature

Country Status (3)

Country Link
FR (1) FR839892A (en)
GB (1) GB487983A (en)
NL (1) NL50752C (en)

Cited By (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434815A (en) * 1943-10-30 1948-01-20 Union Oil Co Method and apparatus for educting oil from oil shale by use of superheated steam
US2466593A (en) * 1944-01-17 1949-04-05 Union Oil Co Multiple stage shale eduction process
US2544843A (en) * 1948-01-28 1951-03-13 Universal Oil Prod Co Treatment of solid hydrocarbonaceous material
US2639263A (en) * 1948-10-05 1953-05-19 Universal Oil Prod Co Method for distilling solid hydrocarbonaceous material
US2647077A (en) * 1949-06-13 1953-07-28 Phillips Petroleum Co Process for destructive distillation
US2656308A (en) * 1950-09-16 1953-10-20 Inst Gas Technology Distillation of oil-shale
US2782158A (en) * 1945-11-02 1957-02-19 John A Wheeler Neutronic reactor
US2812288A (en) * 1950-10-11 1957-11-05 California Research Corp Destructive distillation of hydrocarbonaceous materials
US4140583A (en) * 1976-11-05 1979-02-20 Pioneer Corporation Processing of lignite for petrochemicals
US4431483A (en) * 1981-04-15 1984-02-14 Nippon Kokan Kabushiki Kaisha Apparatus for distilling shale oil from oil shale
CN103205267A (en) * 2013-04-18 2013-07-17 陕西煤业化工技术研究院有限责任公司 Medium and low temperature distillation furnace of coal, distillation device based on distillation furnace, and distillation method
WO2019046469A1 (en) * 2017-08-30 2019-03-07 Pyro Dynamics L.L.C. Apparatus, system, and method for shale pyrolysis
US11111440B1 (en) 2020-02-27 2021-09-07 Pyro Dynamics, Llc Apparatus, system, and method for shale pyrolysis
US11866649B2 (en) 2020-02-27 2024-01-09 Pyro Dynamics, Llc Apparatus, system, and method for shale pyrolysis

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2661327A (en) * 1950-12-04 1953-12-01 Dalin David Apparatus for the destructive distillation of oil shale

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2434815A (en) * 1943-10-30 1948-01-20 Union Oil Co Method and apparatus for educting oil from oil shale by use of superheated steam
US2466593A (en) * 1944-01-17 1949-04-05 Union Oil Co Multiple stage shale eduction process
US2782158A (en) * 1945-11-02 1957-02-19 John A Wheeler Neutronic reactor
US2544843A (en) * 1948-01-28 1951-03-13 Universal Oil Prod Co Treatment of solid hydrocarbonaceous material
US2639263A (en) * 1948-10-05 1953-05-19 Universal Oil Prod Co Method for distilling solid hydrocarbonaceous material
US2647077A (en) * 1949-06-13 1953-07-28 Phillips Petroleum Co Process for destructive distillation
US2656308A (en) * 1950-09-16 1953-10-20 Inst Gas Technology Distillation of oil-shale
US2812288A (en) * 1950-10-11 1957-11-05 California Research Corp Destructive distillation of hydrocarbonaceous materials
US4140583A (en) * 1976-11-05 1979-02-20 Pioneer Corporation Processing of lignite for petrochemicals
US4431483A (en) * 1981-04-15 1984-02-14 Nippon Kokan Kabushiki Kaisha Apparatus for distilling shale oil from oil shale
CN103205267A (en) * 2013-04-18 2013-07-17 陕西煤业化工技术研究院有限责任公司 Medium and low temperature distillation furnace of coal, distillation device based on distillation furnace, and distillation method
CN103205267B (en) * 2013-04-18 2014-07-02 陕西煤业化工技术研究院有限责任公司 Medium and low temperature coal distillation device and distillation method
WO2019046469A1 (en) * 2017-08-30 2019-03-07 Pyro Dynamics L.L.C. Apparatus, system, and method for shale pyrolysis
US10829693B2 (en) 2017-08-30 2020-11-10 Pyro Dynamics LLC Apparatus, system, and method for shale pyrolysis
US11111440B1 (en) 2020-02-27 2021-09-07 Pyro Dynamics, Llc Apparatus, system, and method for shale pyrolysis
US11834612B2 (en) 2020-02-27 2023-12-05 Pyro Dynamics, Llc Apparatus, system, and method for shale pyrolysis
US11866649B2 (en) 2020-02-27 2024-01-09 Pyro Dynamics, Llc Apparatus, system, and method for shale pyrolysis

Also Published As

Publication number Publication date
FR839892A (en) 1939-04-13
NL50752C (en) 1941-08-16

Similar Documents

Publication Publication Date Title
GB487983A (en) Method and apparatus for destructive distillation at low temperature
US1197456A (en) Process of producing power from peat or other carbonaceous matter.
US1822383A (en) Process of making a solid fuel
GB484050A (en) Method and apparatus for destructive distillation at low temperature
US3404960A (en) Continuous process for simultaneously producing coke and carbon black
GB522640A (en) Improvements in the manufacture of combustible gas and coke from carbonaceous materials
US1808672A (en) Process of producing mixed water gas and coal gas
US1426159A (en) Process of producing combustible gas and for carbonizing coal
GB221388A (en) Improvements in processes of carbonizing
GB490264A (en) Improvements in or relating to the low temperature distillation of fuels
US1197804A (en) Method of carbonizing coal.
GB533877A (en) Process for the production of a water gas particularly suitable for synthetic purposes
US1624644A (en) Process of making combustible gas
GB348207A (en)
GB244337A (en) Improved process of and apparatus for producing coke, gas and tar from solid fuel
GB547251A (en) Improvements in the production of carburetted water gas
GB188019A (en) Improvements relating to the distillation of solid carboniferous matter
GB473125A (en) Means of producing gas from tar, crude oils and carbonaceous liquid materials
GB227726A (en) Improvements in and relating to the complete gasification of fuel and the production of high grade gas
GB218925A (en) Improvements in and relating to the carbonisation of coal and the production of high grade gas
GB338369A (en) An improved method of producing carbon dioxide
GB488567A (en) Process of and apparatus for the continuous heat treatment of solid carbonaceous fuels
GB213100A (en) Improvement in apparatus for distilling carbonaceous material
GB288797A (en) Improvements in and relating to the manufacture of water gas
GB143223A (en) Improvements in or relating to destructive distillation of solid combustibles especially of schists, shales, peat, and similar carbonaceous materials