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A method and system for recovering heavy hydrocarbons in liquefied natural gas production

A technology of liquefied natural gas and natural gas, which is applied in the direction of liquid hydrocarbon mixture recovery, hydrocarbon oil, gas fuel, etc., can solve the problems of increased process complexity, incomplete separation, and complicated process flow, so as to improve resource utilization efficiency and increase process efficiency. Effect of adding value and simplifying the process

Inactive Publication Date: 2019-01-04
BEIJING ENCRYO ENG
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  • Application Information

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Problems solved by technology

However, this method has a complicated process and consumes a lot of energy when the absorbent is regenerated.
(3) Condensation separation method: In this method, the natural gas is pre-cooled to -30~-60°C and then separated by one or more stages of heavy hydrocarbon separator. This method is not effective for the separation of aromatic hydrocarbons such as benzene, and is only suitable for the treatment of aromatic hydrocarbons. Natural gas with very low hydrocarbon content, and the separated heavy hydrocarbons are of poor quality and low added value
Chinese patents CN103031169A and CN103351896A both proposed improved schemes on this basis. By setting heavy hydrocarbon scrubbers and deethanizers and / or rectification towers to separate heavy hydrocarbons, the improved schemes improved the performance of the process for removing heavy hydrocarbons, but Due to the need to add more than three separation towers, the complexity of the process is greatly increased
In summary, the existing LNG heavy hydrocarbon removal process has disadvantages such as high energy consumption, incomplete separation, poor applicability, complex process flow, poor quality of recovered heavy hydrocarbons, and low added value. With the rapid growth of the industry, the market urgently needs a more complete new technology for the removal and recovery of heavy hydrocarbons from natural gas liquefaction

Method used

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  • A method and system for recovering heavy hydrocarbons in liquefied natural gas production

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Embodiment 1

[0035] For the specific process flow of this embodiment, please refer to figure 1 .

[0036] A system for recovering heavy hydrocarbons in the production of liquefied natural gas, comprising: a first flow path A, a second flow path B, a third flow path C of a cold box 1, a heavy hydrocarbon removal tower 2, a tower top condenser 3, a bottom re- Boiler 4, heavy hydrocarbon cooler 5, heavy hydrocarbon storage tank 6, first valve V1 to sixth valve V6 and corresponding connecting pipelines, wherein, the inlet of the first flow channel A of the cold box 1 is connected with the raw gas pipeline, and the outlet passes through The second valve V2 is connected to the feed port of the heavy hydrocarbon removal tower 2; the inlet of the second channel B of the cold box 1 is connected to the shell-side gas phase outlet of the tower top condenser 3, and the outlet is connected to the LNG product pipeline through the sixth valve V6 ; The inlet of the third channel C of the cold box 1 is co...

Embodiment 2

[0039] For the specific process flow of this embodiment, please refer to figure 1 .

[0040] The raw natural gas I from the outside is passed into the inlet of the first channel A of the cold box 1. The raw natural gas is natural gas that has been deacidified, dehydrated, demercurized, and rich in heavy hydrocarbons, with a flow rate of 1500kg / h and a pressure of 6.5MPa , the temperature is 38°C, the total content of heavy hydrocarbons is 40ppmv, of which the content of neopentane is 10ppmv, the content of benzene is 10ppmv, and the content of C6 and above hydrocarbons is 20ppmv. After being cooled by the first channel A of the cold box 1, the temperature drops to -80 ℃ to obtain natural gas II in a gas-liquid two-phase state. The natural gas II is decompressed to 6.0 MPa through the second valve V2 and then enters the middle feed port of the heavy hydrocarbon removal tower 2. ℃, with a flow rate of 60.2kg / h of heavy hydrocarbons I, the gas phase outlet of the shell side of t...

Embodiment 3

[0042] For the specific process flow of this embodiment, please refer to figure 1 .

[0043] The raw natural gas I from the outside is passed into the inlet of the first channel A of the cold box 1. The raw natural gas is natural gas that has been deacidified, dehydrated, demercurized, and rich in heavy hydrocarbons, with a flow rate of 15000kg / h and a pressure of 3.5MPa , the temperature is 45°C, the total content of heavy hydrocarbons is 10000ppmv, of which the content of neopentane is 400ppmv, the content of benzene is 600ppmv, and the content of C6 and above hydrocarbons is 9000ppmv. After being cooled by the first channel A of the cold box 1, the temperature drops to -40 ℃ to obtain natural gas II in a gas-liquid two-phase state. The natural gas II is decompressed to 3.0 MPa through the second valve V2 and then enters the middle feed port of the heavy hydrocarbon removal tower 2, and is purified by rectification of the heavy hydrocarbon removal. ℃, with a flow rate of 11...

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Abstract

The invention relates to a method and system for recovering heavy hydrocarbon in liquefied natural gas production.The method comprises the steps that natural gas cooled by a cold box 1 is subjected to rectification through a heavy hydrocarbon removal tower 2 with a tower top condenser 3 and a tower bottom reboiler 4 so as to separate the heavy hydrocarbon; a gas phase subjected to the rectification and separation is condensed at the tower top condenser 3 portion, then a liquid phase drops and returns to the heavy hydrocarbon removal tower 2, the uncondensed gas phase flows into the cold box 1, and further deep cooling is performed to obtain an LNG product I; the liquid phase subjected to stripping distillation is led out of the side face of the heavy hydrocarbon removal tower 2 and fed into the tower bottom reboiler 4, is heated and reboiled and then returns to the heavy hydrocarbon removal tower 2, then the liquid phase is led out of the bottom of the heavy hydrocarbon removal tower 2, cooled by a heavy hydrocarbon cooler 5 and subjected to pressure reduction and then is fed into a heavy hydrocarbon storage tank 6, and the heavy hydrocarbon product is obtained from a liquid phase outlet.In addition, a cold source used in the heavy hydrocarbon removal process is extracted from the LNG product and is fed into the tower top condenser 3 for reheating, then the cold source returns to the cold box 1, and the further deep cooling is performed to obtain an LNG product II.The method makes a heavy hydrocarbon removal process coupled in the natural gas liquefaction process, is high in process integration, good in stability and good in applicability and has very strong operability.

Description

technical field [0001] The invention relates to the field of liquefied natural gas production, in particular to a method and system for recovering heavy hydrocarbons in liquefied natural gas production. Background technique [0002] In view of the many advantages of liquefied natural gas in storage, transportation and use, liquefied natural gas (LNG) has become the development and utilization trend of the natural gas industry, and the demand for liquefied natural gas is rising rapidly. my country's liquefied natural gas has made great progress in the past ten years. However, due to the late start of the liquefied natural gas industry, insufficient technical reserves, and the variety of natural gas sources in my country, many pre-built factories have underestimated the changes in natural gas raw materials, especially the content of components that are prone to freezing and blocking in heavy hydrocarbons, and there has been a lack of heavy hydrocarbon removal devices. Insuffic...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C10L3/10C10G5/00C10G5/06
CPCC10G5/00C10G5/06C10G2300/1025C10L3/10
Inventor 王道广张会军李慧王英军
Owner BEIJING ENCRYO ENG
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