US3261878A - Autothermal cracking of liquid hydrocarbons - Google Patents

Autothermal cracking of liquid hydrocarbons Download PDF

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US3261878A
US3261878A US3261878DA US3261878A US 3261878 A US3261878 A US 3261878A US 3261878D A US3261878D A US 3261878DA US 3261878 A US3261878 A US 3261878A
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fluidized bed
oil coke
cracking
oil
liquid hydrocarbons
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    • 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
    • C10B55/00—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material
    • C10B55/02—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials
    • C10B55/04—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials
    • C10B55/08—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form
    • C10B55/10—Coking mineral oils, bitumen, tar, and the like or mixtures thereof with solid carbonaceous material with solid materials with moving solid materials in dispersed form according to the "fluidised bed" technique
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C11/00—Aliphatic unsaturated hydrocarbons
    • C07C11/02—Alkenes
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/02—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by cracking a single hydrocarbon or a mixture of individually defined hydrocarbons or a normally gaseous hydrocarbon fraction
    • C07C4/025—Oxidative cracking, autothermal cracking or cracking by partial combustion

Definitions

  • This invention relates to a process for the production of gaseous olefines, especially ethylene, from liquid hydrocarbons, and especially to a process for the autothermal cracking of liquid hydrocarbons, for example crude petroleums, in a fluidized bed of oil coke formed by the cracking.
  • the said process is of special importance in processing liquid hydrocarbons with low Conradson carbon, for ex ample with more than 0% up to about 2.5% Conradson carbon, such as crude petroleums having this property, and in the processing of liquid hydrocarbons, especially crude petroleums, which contain water.
  • Conradson carbon such as crude petroleums having this property
  • the formation of oil coke during cracking is usually insuflicient to compensate for the loss by combustion and attrition.
  • a content of salts, especially alkali salts, such as sodium and potassium chloride often favors the combustion of oil coke. It has therefore always been necessary to separate the water by a special purification method prior to the use of such initial hydrocarbons.
  • Liquid hydrocarbons or certain fractions of petroleum 3,261,878 Patented July 19, 1966 distillation, gas oils and mineral oil residues, may be used as initial materials for the process.
  • the process is epecially suitable for processing crude petroleums.
  • the additions which inhibit burning of the oil coke may be substances which contain phosphoric and/ or boric acid or their salts, for example boric acid and phosphoric acid themselves and also the various salts of phosphoric and boric acids, such as sodium, potassium, ammonium, magnesium, calcium, strontium, barium, zinc and aluminum salts.
  • Primary, secondary and also tertiary phosphates i.e., alkali metal and ammonium salts, may be used as phosphates, and also mixed phosphates, for example sodium ammonium phosphate.
  • Ammonium phosphate (NH )H PO is especially suitable.
  • Compounds of boron and phosphorus may be used, as well as mixtures of boric acid and its salts with phosphoric acid and salts of phosphoric acid.
  • 0.05% by weight up to about 6% by weight, preferably 0.2 to 3% :by weight, of these compounds is added with reference to the weight of oil coke present in the fluidized 'bed.
  • the cracking of the liquid hydrocarbons is carried out at temperatures of 630 to 850 C., especially :at 680 to 780 C.
  • the flu-idizing agent may be steam and/ or carbon dioxide or another inert gas, and the oxygen necessary for autothermal cracking may be added thereto.
  • the oxygen necessary for partial combustion may be added in the form of an oxygen-containing gas, for example air. However, it is preferable to add the oxygen in pure form, i.e., a commercially pure oxygen such as is obtained for example by liquefaction of air.
  • Example 1 A fluidized bed of oil coke is supported above a metal grate provided with fine slots arranged in a shaft furnace having a cross-section of 1 sq. m.
  • a mixture of about 400 kg./h. of steam and about 200 m. (S.T.P.) per hour of oxygen is blown upwardly into the fluidized bed.
  • 800 kg. per hour of Sahara crude oil with 0.8% Conradson carbon is sprayed in above the grate.
  • Hydrocarbons boiling above 250 C. formed in the process are returned to the fluidized bed in an amount of 250 kg. per hour immediately above the grate.
  • 1 kg. of primary sodium phosphate is added to the fluidized bed.
  • the ratio of steam and oxygen supplied is regulated so that a reaction temperature of 720 C. prevails in the fluidized bed.
  • Solids entrained from the fluidized bed by the cracking gases and vapors formed are separated in a cyclone provided above the fluidized bed and flow back into the fluidized bed through the discharge pipe of the cyclone.
  • About 4 kg. per hour of excess oil coke is formed and is continuously removed.
  • the phosphorus content of the oil coke in the fluidized bed is 1.4% by weight.
  • Example 2 800 kg. per hour of a crude oil from Upper Alsace (France) with 2.3% Conradson carbon contaminated with 1% by weight of salt water is cracked in a fluidized bed of oil coke in the way described in Example 1. At the same time about 400 kg. per hour of steam and about 200 m. (S.T.P.) of oxygen is supplied. The hydrocarbons boiling above about 250 C. formed by the process are returned to the fluidized bed in an amount of 300 kg. per hour. 100 g. of calcium ammonium phosphate is introduced into the fluidized bed per hour. At a temperature of 730 C. in the fluidized bed, 190 kg. of ethylene, 120 kg.
  • S.T.P. 200 m.
  • An additive containing boron may be used instead of a phosphate as in Example 1.

Description

United States Patent "ice 4 Claims. 61. 260-683) This invention relates to a process for the production of gaseous olefines, especially ethylene, from liquid hydrocarbons, and especially to a process for the autothermal cracking of liquid hydrocarbons, for example crude petroleums, in a fluidized bed of oil coke formed by the cracking.
It is known to crack liquid hydrocarbons for the production of gaseous olefines, especially ethylene, in a fluidized bed of granular solids, "by burning part of the hydrocarbon to be cracked with oxygen to produce the necessary cracking heat and cracking the remainder of the hydrocarbon with or without the addition of steam. The continuous cracking of hydrocarbons in a fluidized bed is in general carried out at temperatures of more than 600 C. and it is advantageous to use for the fluidized bed oil coke formed by the cracking. This oil coke usually forms in globular form, is less corrosive than other inert solids and is less liable to attrition.
.For uniform cracking it is essential that a constant height of the fluidized bed, and consequently a constant content in the fluidized bed of oil coke formed by the cracking to be maintained. It is therefore necessary to carry out the process in such a way that the losses occurring by attrition and combustion are at least compensated for by fresh formation of oil coke. The fresh formation of oil coke during the cracking and the extent of consumption of oil coke already present are dependent on many factors.
We have now found that the equilibrium between the formation of oil coke during cracking and consumption of oil coke by combustion and attrition can be regulated so much in favor of the fresh formation of oil coke and at the expense of consumption of oil coke that decrease in the amount of fluidized solid is prevented by adding to the fluidized bed small amounts of substances which contain phosphoric and/or boric acid or salts of the same.
The said process is of special importance in processing liquid hydrocarbons with low Conradson carbon, for ex ample with more than 0% up to about 2.5% Conradson carbon, such as crude petroleums having this property, and in the processing of liquid hydrocarbons, especially crude petroleums, which contain water. When using crude petroleums with low Conradson carbon, for example in the said range, the formation of oil coke during cracking is usually insuflicient to compensate for the loss by combustion and attrition. In the case of hydrocarbons containing water, for example crude petroleums, a content of salts, especially alkali salts, such as sodium and potassium chloride, often favors the combustion of oil coke. It has therefore always been necessary to separate the water by a special purification method prior to the use of such initial hydrocarbons. By the process according to this invention it is now possible to crack both crude petroleums containing :aqueous solutions of salts and also crude petroleums having low Conradson carbon, autothermally to gaseous olefines and to provide the fluidized bed solely from the oil coke formed by the crackmg.
Liquid hydrocarbons or certain fractions of petroleum 3,261,878 Patented July 19, 1966 distillation, gas oils and mineral oil residues, may be used as initial materials for the process. The process is epecially suitable for processing crude petroleums. The additions which inhibit burning of the oil coke may be substances which contain phosphoric and/ or boric acid or their salts, for example boric acid and phosphoric acid themselves and also the various salts of phosphoric and boric acids, such as sodium, potassium, ammonium, magnesium, calcium, strontium, barium, zinc and aluminum salts. Primary, secondary and also tertiary phosphates, i.e., alkali metal and ammonium salts, may be used as phosphates, and also mixed phosphates, for example sodium ammonium phosphate. Ammonium phosphate (NH )H PO is especially suitable. Compounds of boron and phosphorus may be used, as well as mixtures of boric acid and its salts with phosphoric acid and salts of phosphoric acid.
In general, 0.05% by weight up to about 6% by weight, preferably 0.2 to 3% :by weight, of these compounds is added with reference to the weight of oil coke present in the fluidized 'bed. The cracking of the liquid hydrocarbons is carried out at temperatures of 630 to 850 C., especially :at 680 to 780 C. The flu-idizing agent may be steam and/ or carbon dioxide or another inert gas, and the oxygen necessary for autothermal cracking may be added thereto. The oxygen necessary for partial combustion may be added in the form of an oxygen-containing gas, for example air. However, it is preferable to add the oxygen in pure form, i.e., a commercially pure oxygen such as is obtained for example by liquefaction of air. It has proved to be advantageous to mix a part of the oxygen necessary for cracking with the initial materials, for example the crude oil, prior to the same being introduced into the fluidized bed, and to introduce the mixture direct into the fluidized bed. For this introduction it is essential that the oxygen should be mixed completely with the initial hydrocarbon by appropriate apparatus. One or more suitable multi-substance nozzles may, for example, be used, to achieve intimate mixing of the hydrocarbon with the oxygen.
In carrying out the process it is advantageous to return at least part of the high boiling oils containing up to 50% by weight of asphalts arising in the cracking to the fluidized bed. It is especially advantageous to return the fraction or a part of the fraction boiling above 250 C. of the oil formed by cracking.
The invention is illustrated by, but not limited to, the following examples.
Example 1 A fluidized bed of oil coke is supported above a metal grate provided with fine slots arranged in a shaft furnace having a cross-section of 1 sq. m. A mixture of about 400 kg./h. of steam and about 200 m. (S.T.P.) per hour of oxygen is blown upwardly into the fluidized bed. 800 kg. per hour of Sahara crude oil with 0.8% Conradson carbon is sprayed in above the grate. Hydrocarbons boiling above 250 C. formed in the process are returned to the fluidized bed in an amount of 250 kg. per hour immediately above the grate. Periodically, at intervals of 4 hours, 1 kg. of primary sodium phosphate is added to the fluidized bed. The ratio of steam and oxygen supplied is regulated so that a reaction temperature of 720 C. prevails in the fluidized bed. Solids entrained from the fluidized bed by the cracking gases and vapors formed are separated in a cyclone provided above the fluidized bed and flow back into the fluidized bed through the discharge pipe of the cyclone. About 4 kg. per hour of excess oil coke is formed and is continuously removed. In the stationary state, the phosphorus content of the oil coke in the fluidized bed is 1.4% by weight.
The same amount of oil coke is formed when 500 g. of boric acid is added every four hours instead of 1 kg. of
primary sodium phosphate. In the stationary state the boron content of the oil coke is then 0.5% by weight.
About 200 kg. of ethylene and 100 kg. of propylene are formed from each metric ton of fresh oil. 700 m. (S.T.P.) of gas of the calorific value 7200 kcaL/m. and a gasoline rich in aromatics as well as oil 'coke are also formed.
When working under the same experimental conditions but without the supply of primary sodium phosphate or boric acid, no excess of oil coke is formed. On the contrary, the amount of oil coke decreases by 30 kg. per hour in the fluidized bed so that it is not possible to carry out the advantageous operation with a fluidized bed of oil coke formed by the process itself.
Example 2 800 kg. per hour of a crude oil from Upper Alsace (France) with 2.3% Conradson carbon contaminated with 1% by weight of salt water is cracked in a fluidized bed of oil coke in the way described in Example 1. At the same time about 400 kg. per hour of steam and about 200 m. (S.T.P.) of oxygen is supplied. The hydrocarbons boiling above about 250 C. formed by the process are returned to the fluidized bed in an amount of 300 kg. per hour. 100 g. of calcium ammonium phosphate is introduced into the fluidized bed per hour. At a temperature of 730 C. in the fluidized bed, 190 kg. of ethylene, 120 kg. of propylene, 650 m5 (S.T.P.) of a gas having a calorific value of 7400 kcal. per m. and a gasoline rich in aromatics as well as 5 kg. of oil coke are obtained from 1 metric ton of crude oil.
An additive containing boron may be used instead of a phosphate as in Example 1. The same amount of oil coke-5 kg. per metric ton of crude oil-is formed when introducing 40 g. of boric acid per hour into the fluidized bed instead of 100 g. of calcium ammonium phosphate.
If the addition of phosphate or boric acid is omitted. no excess oil coke forms. On the contrary, the amount of oil coke contained in the fluidizedv bed decreases by i about 16 kg. per hour so that continuous operation cannot be maintained without adding extraneous coke.
We claim:
1. In a method for the autothermal cracking of liquid hydrocarbons for the production of gaseous olefines in a fluidized bed of oil coke formed by the cracking at temperatures of 630 to 850 C. in the presence of oxygen and steam, the improvement which comprises adding to the oil coke in the fluidized bed from 0.05 to about 6% by weight based on the amount of said oil coke of a compound selected from the group consisting of phosphoric acid, boric acid, a salt of phosphoric acid, a salt of boric acid and mixtures thereof.
2. The method of claim 1 wherein ammonium phosphate is added to the oil coke in the fluidized bed.
3. The method of claim 1, wherein sodium ammonium phosphate is added to the oil coke in the fluidized bed.
4. In a method for the autothermal cracking of liquid hydrocarbons for the production of gaseous olefines in a fluidized bed. of oil coke formed by the cracking at temperatures of 680 to 780 C. in the presence of oxygen and steam, the improvement which comprises adding to the oil coke in the fluidized bed from 0.2 to about 3% by weight based on the amount of said oil coke of a compound selected from the group consisting of phosphoric acid, boric acid, a salt of phosphoric acid, a salt of boric acid and mixtures thereof.
References Cited by the Examiner UNITED STATES PATENTS 2,564,268 8/1951 Mathy et al 208114 2,587,703 3/1952 Deanesly 2087 3,027,415 3/1962 Steinhofer et a1. 260683 DELBERT E. GANTZ, Primary Examiner.
ALPHONSO D. SULLIVAN, Examiner.
P. M. COUGHLAN, C. E. SPRESSER,
Assislarzt Examiners.

Claims (1)

1. IN A METHOD FOR THE AUTOTHERMAL CRACKING OF LIQUID HYDROCARBONS FOR THE PRODUCTION OF GASEOUS OLEFINES IN A FLUIDIZED BED OF OIL COKE FORMED BY THE CRACKING AT TEMPERATURES OF 630 TO 850*C. IN THE PRESENCE OF OXYGEN AND STEAM, THE IMPROVEMENT WHICH COMPRISES ADDING TO THE OIL COKE IN THE FLUIDIZED BED FROM 0.05 TO ABOUT 6% BY WEIGHT BASED ON THE AMOUNT OF SAID OIL COKE OF A COMPOUND SELECTED FROM THE GROUP CONSISTING OF PHOSPHORIC ACID, BORIC ACID, A SLAT OF PHOSPHORIC ACID, A SALT OF BORIC ACID AND MIXTURES THEREOF.
US3261878D 1961-02-09 Autothermal cracking of liquid hydrocarbons Expired - Lifetime US3261878A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4370223A (en) * 1980-12-31 1983-01-25 Chevron Research Company Coking hydrocarbonaceous oils with an aqueous liquid
US4504382A (en) * 1982-10-14 1985-03-12 Exxon Research And Engineering Co. Phosphorus-containing catalyst and catalytic cracking process utilizing the same
EP0207745A2 (en) * 1985-06-27 1987-01-07 Betz Europe, Inc. Composition and method for coke retardant during hydrocarbon processing
US20050126107A1 (en) * 2002-04-12 2005-06-16 Colman Derek A. Support grid

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US4430199A (en) 1981-05-20 1984-02-07 Engelhard Corporation Passivation of contaminant metals on cracking catalysts by phosphorus addition
US10603657B2 (en) 2016-04-11 2020-03-31 Saudi Arabian Oil Company Nano-sized zeolite supported catalysts and methods for their production
US11084992B2 (en) 2016-06-02 2021-08-10 Saudi Arabian Oil Company Systems and methods for upgrading heavy oils
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US10870802B2 (en) 2017-05-31 2020-12-22 Saudi Arabian Oil Company High-severity fluidized catalytic cracking systems and processes having partial catalyst recycle
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US10889768B2 (en) 2018-01-25 2021-01-12 Saudi Arabian Oil Company High severity fluidized catalytic cracking systems and processes for producing olefins from petroleum feeds
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US11242493B1 (en) 2020-09-01 2022-02-08 Saudi Arabian Oil Company Methods for processing crude oils to form light olefins
US11505754B2 (en) 2020-09-01 2022-11-22 Saudi Arabian Oil Company Processes for producing petrochemical products from atmospheric residues
US11332680B2 (en) 2020-09-01 2022-05-17 Saudi Arabian Oil Company Processes for producing petrochemical products that utilize fluid catalytic cracking of lesser and greater boiling point fractions with steam
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Citations (3)

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Publication number Priority date Publication date Assignee Title
US2564268A (en) * 1947-11-10 1951-08-14 Phillips Petroleum Co Catalytic oil cracking
US2587703A (en) * 1948-02-18 1952-03-04 Universal Oil Prod Co Cracking heavy oils in presence of oxygen
US3027415A (en) * 1958-03-19 1962-03-27 Production of unsaturated hydrocarbons

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2564268A (en) * 1947-11-10 1951-08-14 Phillips Petroleum Co Catalytic oil cracking
US2587703A (en) * 1948-02-18 1952-03-04 Universal Oil Prod Co Cracking heavy oils in presence of oxygen
US3027415A (en) * 1958-03-19 1962-03-27 Production of unsaturated hydrocarbons

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4370223A (en) * 1980-12-31 1983-01-25 Chevron Research Company Coking hydrocarbonaceous oils with an aqueous liquid
US4504382A (en) * 1982-10-14 1985-03-12 Exxon Research And Engineering Co. Phosphorus-containing catalyst and catalytic cracking process utilizing the same
EP0207745A2 (en) * 1985-06-27 1987-01-07 Betz Europe, Inc. Composition and method for coke retardant during hydrocarbon processing
US4663018A (en) * 1985-06-27 1987-05-05 Betz Laboratories, Inc. Method for coke retardant during hydrocarbon processing
EP0207745A3 (en) * 1985-06-27 1988-02-10 Betz Europe, Inc. Composition and method for coke retardant during hydrocarbon processing
US20050126107A1 (en) * 2002-04-12 2005-06-16 Colman Derek A. Support grid

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GB978576A (en) 1964-12-23
DE1133362B (en) 1962-07-19
FR1314261A (en) 1963-01-04

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