LU102381B1 - A Recovery Device for Retorting Gas Light Oil in Induction Adsorption and Desorption Oil Shale - Google Patents

A Recovery Device for Retorting Gas Light Oil in Induction Adsorption and Desorption Oil Shale Download PDF

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Publication number
LU102381B1
LU102381B1 LU102381A LU102381A LU102381B1 LU 102381 B1 LU102381 B1 LU 102381B1 LU 102381 A LU102381 A LU 102381A LU 102381 A LU102381 A LU 102381A LU 102381 B1 LU102381 B1 LU 102381B1
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LU
Luxembourg
Prior art keywords
gas
oil
circulation tank
synchronous circulation
inlet
Prior art date
Application number
LU102381A
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French (fr)
Inventor
Li Bai
Xiuling Xu
Yan Shi
Mingshu Chi
Original Assignee
Univ Jilin Jianzhu
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Priority to LU102381A priority Critical patent/LU102381B1/en
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Publication of LU102381B1 publication Critical patent/LU102381B1/en

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    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B19/00Heating of coke ovens by electrical means
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10BDESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/06Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of oil shale and/or or bituminous rocks
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING 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
    • C10G1/00Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/04Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal by extraction

Abstract

A recovery device for retorting gas light oil in induction adsorption and desorption oil shale is provided, wherein oily gas inlets of two synchronous circulation tanks are connected with an oily gas source; gas outlets of two synchronous circulation tanks are connected with a gas inlet of the gas storage tank; a gas outlet of the gas storage tank is connected with the gas inlets of the synchronous circulation tanks, respectively; the oil and gas outlets of the synchronous circulation tanks are connected with an inlet of the circulating pump, an outlet of the circuiting pump is connected with a gas inlet of the gas storage tank and a gas inlet of the gas condenser, respectively.

Description

A Recovery Device for Retorting Gas Light Oil in Induction Adsorption and Desorption Oil Shale
TECHNICAL FIELD The present invention refers to the retorting and refining technology field of oil shale, and provides a recovery device for retorting gas light oil in induction adsorption and desorption oil shale.
BACKGROUND Retorting of oil shale means that the oil shale is heated to the required temperature in an air-isolated environment, resulting in the pyrolytic reaction of the parent material of oil and the formation of retorting products - shale oil and retorting gas. The shale oil can not only be directly used as liquid fuels for marine turbines, but also can be used to produce liquid fuels such as gasoline and diesel oil through rectification process. At present, for the recovery of the shale oil in the industry, the method of condensing and separating the retorting oil and gas is generally adopted. The retorting oil and gas are treated with cooling, so that the shale oil becomes liquid and precipitate, and the remaining gas is non-condensable gas. Therefore, the lower the cooling temperature of the retorting gas is, the more shale oil is condensed and the higher the oil recovery rate is. However, there is a large amount of gas that needs to be condensed in the retorting process. Moreover, with the decrease of oil content per unit of gas, the condensation temperature also decreases and the cooling amount that needs to be used also increases, which is bound to consume a lot of energy. At present, considering the overall economy in the industry, the final temperature of shale oil recovery process is controlled at 40-60°C. If the temperature is lower, more energy will be consumed and oil cost will be increased. This directly results in a large amount of unrecovered light oil in the gas of the final retorting product. On the other hand, the shale oil is a mixture of various hydrocarbons. From its physical and chemical characteristics, it can be seen that its light component (light diesel oil) has a high partial pressure of vapor at room temperature and is highly volatile. It is easy to be adulterated in the retorting gas, which is difficult to be collected, and there will be a phenomenon of gas with oil. The measured data show that the oil content in the gas of a large retorting and refining enterprise in northeast China is 20-25g/Nm?, and the gas output at the outlet of single retorting device is about 70,000- 80,000Nm*/h. In the 24-hour gas discharge, nearly 36 tons of light oil (light diesel oil) is not recovered and is discharged along with the gas exhaust. According to the average statistics in the industry, the oil content in the retorting gas discharged by oil shale enterprises is about 15-20g/Nm°. Such a large amount of high-quality fuel oil has not been recovered, which not only causes huge waste of resources for refining enterprises, but also causes serious pollution to the environment. Moreover, it also causes potential fire hazard to the production environment and harms the production and personal safety.
The carbon fiber is composed of flake graphite microcrystal and other organic fibers stacked along the axial direction of the fiber. The microcrystalline graphite material obtained by high-temperature carbonization and graphitization has good conductivity and thermal conductivity. Due to its highly developed microporous structure, large adsorption capacity, fast desorption and good purification effect, it is characterized by heat resistance, acid resistance and alkali resistance. The carbon fiber has a wide range of adsorption, and large capacity; the adsorption capacity of gasoline, aldehydes, phenols, alcohols, olefins and other organic vapors is several times to dozens of times greater than the activated carbon, and the oil adsorption capacity is many times greater than the activated carbon. It is characterized by small adsorption resistance, fast speed, rapid and complete desorption.
The induction heating is characterized in that an alternating magnetic field is generated by alternating current, and this alternating magnetic field causes an eddy in the conductive material therein, so that the conductive material heats up rapidly. It has the characteristics of fast heating speed, small heat loss and convenient operation, which can not only shorten the process time, improve productivity and reduce cost, but also improve the heating quality of products. According to its working principle, the heat generated by induction heating is generated inside the conductive material, and the heating element is just the conductive material body. Therefore, the induction heating has uniform heating effect, which is beneficial for improving the overall heating effect of the heated body. Because the conductive material body is also heated, the heating time is greatly shortened and the heating efficiency is high. Meanwhile, the induction heating has small thermal inertia, can be started or stopped at any time, and without preheating, it can realize the fast control of temperature rise and drop. and is easy to realize the automatic control of continuous production.
In the oil shale industry, it has not been reported that the efficient recovery technology of shale oil can be achieved by the organic combination of carbon fiber adsorption technology and induction heating regeneration technology.
SUMMARY
The purpose of the present invention is to overcome the deficiency of the existing technology and make substantial innovation to the existing technology, so as to provide a recovery device for retorting gas light oil in induction adsorption and desorption oil shale, with reasonable structure, low cost, high recovery rate and good quality.
The technical solution adopted to realize the purpose of the present invention is as follows: a recovery device for retorting gas light ail in induction adsorption and desorption oil shale, comprising a first synchronous circulation tank, a second synchronous circulation tank, a gas condenser, a light oil storage tank, an induction heating controller, an induction generator, a gas storage tank, a cooling tower and a circulating pump, wherein oily gas inlets on the bottom of the first synchronous circulation tank and the second synchronous circulation tank are connected with an oily gas source; gas outlets on the top of the first synchronous circulation tank and the second synchronous circulation tank are connected with a gas inlet of the gas storage tank; a gas outlet of the gas storage tank is connected with the gas inlets on the top of the first synchronous circulation tank and the second synchronous circulation tank, respectively; the oil and gas outlets on the bottom of the first synchronous circulation tank and the second synchronous circulation tank are connected with an inlet of the circulating pump, an outlet of the circuiting pump is connected with a gas inlet of the gas storage tank and a gas inlet on the top of the gas condenser, respectively, a gas outlet on the bottom of the gas condenser is connected with a gas inlet of the gas storage tank, a water inlet of the cooling and circulating water pipe in the gas condenser is connected with a water inlet on the top of the cooling tower, a water inlet of the cooling and circulating water pipe in the gas condenser is connected with a water outlet on the bottom of the cooling tower, an oil discharge outlet of the gas condenser is connected with an oil inlet of the light oil storage tank, the first synchronous circulation tank and the second synchronous circulation tank are all equipped with a packing layer, the first synchronous circulation tank and the second synchronous circulation tank are all placed in an induction generator, and the induction generator is connected with an induction heating controller.
The packing layer in the first synchronous circulation tank and the second synchronous circulation tank is carbon fiber or graphite particles.
A recovery device for retorting gas light oil in induction adsorption and desorption oil shale of the present invention has the following advantages: (1) As the technology of carbon fiber or graphite particie adsorption and induction heating regeneration is adopted, the light shale oil in the gas can be recovered efficiently; the production and quality of shale oil are greatly improved by separating the light shale oil from the oily gas through efficient circulation; (2) The recycling device adopts two sets of positive and negative cycles, and the recycling process is implemented alternately. The recycling work steps are continuous and stable, which does not affect the whole retorting production process; (3) It makes full use of adsorption and induction heating desorption technology of the carbon fiber or graphite particles, and completely avoid the secondary pollution of the carbon fiber or graphite particles in the regeneration process; meanwhile, as the induction heating temperature is controllable and the heating effect is concentrated, the original structure of the carbon fiber or graphite particles is less damaged, the loss of the carbon fiber or graphite particles is reduced, and the consumption of the carbon fiber or graphite particles is slowed down, which is conducive to the long-term stable work of the device and the production cost is reduced: (4) By using the induction heating regeneration technology, it has the characteristics of fast heating speed, small heat loss and convenient operation, which can not only shorten the recovery time, improve productivity and reduce cost, but also improve the quality of products.
(5) It purifies the gas while obtaining the light shale oil or light diesel oil, which provides a good foundation for the efficient utilization of various retorting products.
(6) The device is characterized of simple structure, obvious separation effect, small investment in construction and implementation, easy to be overhauled and maintained, and it is suitable for the transformation of old technology and the implementation of new process; (7) The device can also be used in the retorting of coal, oil sands, waste tires, petroleum coke, organic waste and biomass.
BRIEF DESCRIPTION OF THE FIGURES Fig. 1 shows a structure diagram of a recovery device for retorting gas light oil in induction adsorption and desorption oil shale of the present invention.
In the figure: 1: the first synchronous circulation tank, 2: the second synchronous circulation tank, 3: the gas condenser, 4: the light oil storage tank,
5: the induction heating controller, 6: the induction heating generator, 7: the gas storage tank, 8: the cooling tower and 9: the circulating pump
DESCRIPTION OF THE INVENTION The present invention is further illustrated in conjunction with figures and embodiments.
As shown in Fig. 1, a recovery device for retorting gas light oil in induction adsorption and desorption oil shale of the present invention, comprising a first synchronous circutation tank 1, a second synchronous circulation tank 2, a gas condenser 3, a light oil storage tank 4, an induction heating controller 5, an induction generator 6, a gas storage tank 7, a cooling tower 8 and a circulating pump 9, wherein oily gas inlets on the bottom of the first synchronous circulation tank 1 and the second synchronous circulation tank 2 are connected with an oily gas source; gas outlets on the top of the first synchronous circulation tank 1 and the second synchronous circulation tank 2 are connected with a gas inlet of the gas storage tank; a gas outlet of the gas storage tank 7 is connected with the gas inlets on the top of the first synchronous circulation tank 1 and the second synchronous circulation tank 2, respectively; oil and gas outlets on the bottom of the first synchronous circulation tank 1 and the second synchronous circulation tank 2 are connected with an inlet of the circulating pump 9, an outlet of the circuiting pump 9 is connected with a gas inlet of the gas storage tank 7 and a gas inlet on the top of the gas condenser 3, respectively; a gas outlet on the bottom of the gas condenser 3 is connected with a gas inlet of the gas storage tank 7, a water inlet of the cooling and circulating water pipe in the gas condenser 3 is connected with a water inlet on the top of the cooling tower 8, a water inlet of the cooling and circulating water pipe in the gas condenser 3 is connected with a water outlet on the bottom of the cooling tower 8, an oil discharge outlet on the bottom of the gas condenser 3 is connected with an oil inlet of the light oil storage tank 4, the first synchronous circulation tank 1 and the second synchronous circulation tank 2 are all equipped with a packing layer, and the first synchronous circulation tank 1 and the second synchronous circuiation tank 2 are all placed in an induction generator 6. The induction generator 6 is connected with an induction heating controller 5. The packing layer in the first synchronous circulation tank 1 and the second synchronous circulation tank 2 is carbon fiber or graphite particles. The induction generator 6 and the connected induction heating controller 5 are commercially available supporting products.
A recovery device for retorting gas light oil in induction adsorption and desorption oil shale of the present invention is only a concrete embodiment and not exhaustive. The technical personnel in this field shall fall within the scope protected by the claims of the present invention without being copied and improved through creative labor.

Claims (2)

Claims
1. A recovery device for retorting gas light oil in induction adsorption and desorption oil shale is characterized in comprising technical solutions as following:a recovery device for retorting gas light oil in induction adsorption and desorption oil shale, comprising a first synchronous circulation tank, a second synchronous circulation tank, a gas condenser, a light oil storage tank, an induction heating controller, an induction generator, a gas storage tank, a cooling tower and a circulating pump, wherein oily gas inlets on the bottom of the first synchronous circulation tank and the second synchronous circulation tank are connected with an oily gas source; gas outlets on the top of the first synchronous circulation tank and the second synchronous circulation tank are connected with a gas inlet of the gas storage tank; a gas outlet of the gas storage tank is connected with the gas inlets on the top of the first synchronous circulation tank and the second synchronous circulation tank, respectively; the oil and gas outlets on the bottom of the first synchronous circulation tank and the second synchronous circulation tank are connected with an inlet of the circulating pump, an outlet of the circuiting pump is connected with a gas inlet of the gas storage tank and a gas inlet on the top of the gas condenser, respectively; a gas outlet on the bottom of the gas condenser is connected with a gas inlet of the gas storage tank, a water inlet of the cooling and circulating water pipe in the gas condenser is connected with a water inlet on the top of the cooling tower, a water inlet of the cooling and circulating water pipe in the gas condenser is connected with a water outlet on the bottom of the cooling tower, an oil discharge outlet of the gas condenser is connected with an oil inlet of the light oil storage tank, the first synchronous circulation tank and the second synchronous circulation tank are al! equipped with a packing layer, the first synchronous circulation tank and the second synchronous circulation tank are all placed in an induction generator, and the induction generator is connected with an induction heating controller.
2. According to claim 1, a recovery device for retorting gas light oil in induction adsorption and desorption oil shale is characterized in that the packing layer in the first synchronous circulation tank and the second synchronous circulation tank is carbon fiber or graphite particles.
LU102381A 2021-01-04 2021-01-04 A Recovery Device for Retorting Gas Light Oil in Induction Adsorption and Desorption Oil Shale LU102381B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
LU102381A LU102381B1 (en) 2021-01-04 2021-01-04 A Recovery Device for Retorting Gas Light Oil in Induction Adsorption and Desorption Oil Shale

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
LU102381A LU102381B1 (en) 2021-01-04 2021-01-04 A Recovery Device for Retorting Gas Light Oil in Induction Adsorption and Desorption Oil Shale

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LU102381B1 true LU102381B1 (en) 2021-08-30

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Effective date: 20210830