High-efficiency heat-integrated moving-bed methanol-to-hydrocarbon process

A methanol-to-hydrocarbon, moving-bed technology, applied in the direction of hydrocarbon production from oxygen-containing organic compounds, condensation between hydrocarbons and non-hydrocarbons, chemical recovery, etc., can solve the problem of wide product distribution, affecting the efficiency of gas-solid separation system, running damage

Active Publication Date: 2017-05-03
CHINA KUNLUN CONTRACTING & ENG
View PDF6 Cites 0 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0007] (1) The degree of back-mixing of the catalyst in the fluidized bed is relatively heavy, and excessive local reaction can easily lead to coking; (2) The turbulence in the fluidized bed is severe, the wear is serious, and the expensive catalyst is easily damaged and then runs out, resulting in economical problems. (3) The residence time distribution in the fluidized bed is wide, which easily leads to a wide distribution of products and a decrease in the yield of the target product; (4) Temperature and pressure fluctuations will affect the efficiency of the gas-solid separation system, thereby affecting the subsequent Fractional distillation system; (5) For the reaction system with low coke formation rate, it is difficult to maintain the heat balance of the reaction regeneration system of the fluidized bed

Method used

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
View more

Image

Smart Image Click on the blue labels to locate them in the text.
Viewing Examples
Smart Image
  • High-efficiency heat-integrated moving-bed methanol-to-hydrocarbon process
  • High-efficiency heat-integrated moving-bed methanol-to-hydrocarbon process
  • High-efficiency heat-integrated moving-bed methanol-to-hydrocarbon process

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0046] Embodiment one (see figure 1 ): Containing the first and second two reactors, the separation step adopts depentanizer fractionation.

[0047] The fresh methanol feed is pumped outside the boundary area, the pressure is increased to 0.5MPaG, and the temperature is 25°C. Fresh methanol feed 1 first enters the first reactor (equivalent to the initial reactor) after heat exchange with the reaction product, and conducts a radial moving bed contact reaction with the highly active catalyst from the regenerator. The liquid hourly space velocity is 1.0 h -1 , to generate an intermediate product (ie, the reaction product of the first reactor), with a pressure of 0.46MPaG and a temperature of 520°C. After leaving the first reactor, the intermediate product enters the first heat exchange unit, which is used as a heat source to heat the feed to the first reactor. The methanol feed 1 is heated to 480°C, and the intermediate product is cooled to 490°C. The intermediate product ente...

Embodiment 2

[0052] Embodiment two (see figure 2 ): Containing the first and second two reactors, the separation step adopts two-stage fractionation of a depentanizer and a debutanizer.

[0053] The fresh methanol feed is pumped through the boundary area, the pressure is increased to 1.77MPaG, and the temperature is 30°C. Fresh methanol feed 1 first enters the first reactor (equivalent to the initial reactor) after heat exchange with the reaction product, and conducts a radial moving bed contact reaction with the highly active catalyst from the regenerator. The liquid hourly space velocity is 5.0 h -1 , generate an intermediate product (ie the reaction product of the first reactor), the pressure is 1.75MPaG, and the temperature is 350°C, or 320°C. After the intermediate product leaves the first reactor, the first heat exchange unit serves as a heat source to heat the feed to the first reactor. The methanol feed is heated to 270°C or 250°C, and the intermediate product is cooled to 320°C...

Embodiment 3

[0059] Embodiment three (see image 3 ): Including the first and second two reactors, the separation step adopts depentanizer and debutanizer two-stage fractional distillation, and uses dehydrogenation reactor to dehydrogenate C3~C4, methanol raw material is divided into two stocks and enters two a reactor.

[0060] The fresh methanol feed 1 is pumped through the boundary area, and the pressure is increased to 0.3MPaG, and the temperature is 30°C. The fresh methanol feed 1 is divided into two stocks after heat exchange with the reaction product: raw material 1 and raw material 2, which are respectively used as the first reactor (equivalent to the initial reactor), the second reactor (equivalent to the final reactor) ) feed, the flow ratio is 9:1. Raw material 1 enters the first reactor, and conducts radial moving bed contact reaction with the highly active catalyst from the regenerator, with a liquid hourly space velocity of 2.5h -1 , generate an intermediate product (ie th...

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

PUM

No PUM Login to view more

Abstract

The invention relates to an efficient heat-integrated method for preparing hydrocarbon from methanol by adopting a moving bed. The method comprises a hydrocarbon synthesis step, a separation step and an after-treatment step, wherein in the hydrocarbon synthesis step, two reactors which are connected with each other in series are adopted; reaction products of a plurality of reactors are utilized to perform heat-exchange heating on reaction raw materials and low-carbon-hydrogen containing recycle gas produced in the separation step, so that the recycle gas is returned to different feeding positions of the hydrocarbon synthesis step as quenching gas or raw material supplementing gas of the hydrocarbon synthesis step; the raw material methanol is utilized to perform scrubbing-absorption on C1-C4 light components generated in the separation step, and returned for being fed and converted, so that the methanol is transformed into high value-added stable light hydrocarbon comprising mixed aromatic hydrocarbons. According to the method, the refining control on a reaction process is improved through inter-stage heat exchange of reaction prdocuts, so that the materials are effectively utilized and thermally integrated among processing processes, and the environmental pollution is reduced while the product yield is increased and the energy consumption is reduced.

Description

technical field [0001] The invention relates to a process for producing hydrocarbons from methanol using a moving bed, and the heat of reaction products in the process can be efficiently circulated and utilized. Background technique [0002] BTX aromatics (Benzene, Toluene, Xylene) are important basic raw materials in petrochemical industry, among which p-xylene (PX) has the greatest demand. With the rapid expansion of domestic PX downstream PTA and polyester production capacity, the supply of PX in the market is seriously insufficient. By 2013, my country's external dependence on p-xylene has reached 55.3%, and the gap between supply and demand has further increased. The PX project produced by the traditional process is difficult to construct, has a high production technology threshold, and requires a large investment, and is more limited by the raw material naphtha resources. At present, the shortage of oil resources in my country and the increase in consumption demand ha...

Claims

the structure of the environmentally friendly knitted fabric provided by the present invention; figure 2 Flow chart of the yarn wrapping machine for environmentally friendly knitted fabrics and storage devices; image 3 Is the parameter map of the yarn covering machine
Login to view more

Application Information

Patent Timeline
no application Login to view more
Patent Type & Authority Patents(China)
IPC IPC(8): C07C1/20C07C2/86C07C15/02
CPCY02P20/584
Inventor 周华堂许贤文李盛兴劳国瑞刘林洋孙富伟李利军卢秀荣丰存礼黄科
Owner CHINA KUNLUN CONTRACTING & ENG
Who we serve
  • R&D Engineer
  • R&D Manager
  • IP Professional
Why Eureka
  • Industry Leading Data Capabilities
  • Powerful AI technology
  • Patent DNA Extraction
Social media
Try Eureka
PatSnap group products