Reactor for synthesizing dimethyl ether by biomass synthesis gas through one-step method and temperature control system

A technology of temperature control system and reactor, which is applied in the field of reactor system, can solve problems such as difficult to scale up and large latent heat, and achieve the effects of low system maintenance cost, high conversion efficiency and good stability

Active Publication Date: 2009-04-01
GUANGZHOU INST OF ENERGY CONVERSION - CHINESE ACAD OF SCI
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  • Abstract
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  • Claims
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Problems solved by technology

[0009] The purpose of the present invention is to overcome the heat transfer limitation of the dimethyl ether fixed bed reactor and its temperature control integrated process system. Problems that are

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  • Reactor for synthesizing dimethyl ether by biomass synthesis gas through one-step method and temperature control system
  • Reactor for synthesizing dimethyl ether by biomass synthesis gas through one-step method and temperature control system
  • Reactor for synthesizing dimethyl ether by biomass synthesis gas through one-step method and temperature control system

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Example Embodiment

[0026] Example:

[0027] like Figure 1 to Figure 3 As shown, the reactor and temperature control system for the one-step synthesis of dimethyl ether from biomass synthesis gas in this embodiment is mainly composed of a steam drum 15 , a boiler 16 and a fixed bed reactor 17 . The fixed-bed reactor 17 is a tubular fixed-bed reactor. In the fixed-bed reactor 17, 36 reaction tubes 8 are distributed in parallel along the longitudinal direction of the reactor 17. The diameter of the reaction tubes 8 is 40 mm, and the adjacent The distance D between the cores of the two reaction tubes 8 is 2.5 times the diameter d of the reaction tubes 8, which is 100 mm in this embodiment; a reaction gas inlet 1 is provided at the top of the fixed-bed reactor 17, and the reactor near the top is The shell side 9 of 17 is provided with an exhaust port 5, and a superheated water outlet 6 is provided on both sides of the reactor 17 close to the exhaust port 5; the bottom end of the fixed-bed reactor 1...

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Abstract

The invention discloses a reactor for one-step preparation of dimethyl ether from biomass syngas, which comprises a fixed bed reactor, a plurality of reaction tubes are parallelly distributed in the reactor along the longitudinal direction; a reaction gas inlet is arranged at the top end of the fixed bed reactor, an exhaust outlet is arranged on a shell pass of the reactor which is near to the top end, overheated water outlets are arranged at the two sides of the reactor which are near to the exhaust outlet; a reaction gas outlet is arranged at the bottom end of the fixed-bed reactor, a liquid drainage port is arranged on the shell pass of the reactor which is near to the bottom end, and overheated water inlets are arranged on the two sides of the reactor which are near to the liquid drainage port. The reactor overcomes the shortcoming that the traditional fixed bed reactor is difficult to enlarge due to the thermal transfer limitation, makes full use of the advantages of high conversation efficiency, simple operation, good stability, low investment, low system maintenance cost, and the like of the fixed-bed reactor, designs a one-step dimethyl ether synthesis device with the larger scale and rapidly promotes the marketization of the technology of synthesizing liquid fuel from the biomass syngas.

Description

technical field [0001] The invention provides a reactor system for preparing high-grade liquid fuel from biomass synthesis gas, in particular to a reactor for one-step production of dimethyl ether from biomass synthesis gas and a precise temperature control system thereof. Background technique [0002] Dimethyl ether is a chemical product with a wide range of uses. It can replace chlorofluorocarbons as aerosol sprays and environmentally friendly refrigerants. It is also an important raw material for the production of low-carbon olefins. Studies in recent years have shown that DME can be directly used as fuel as a substitute for liquefied petroleum gas and diesel. Therefore, the potential market for DME is undoubtedly huge. [0003] At present, the industrial production of DME mainly adopts methanol catalytic dehydration process, which has a small scale and high production cost. The large-scale production of DME should adopt the direct conversion process of synthesis gas. ...

Claims

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Application Information

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IPC IPC(8): C07C43/04C07C41/01
Inventor 王铁军周华张兴华吴创之马隆龙张琦
Owner GUANGZHOU INST OF ENERGY CONVERSION - CHINESE ACAD OF SCI
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