Process for producing alcohol-ether hydrazine under medium/low-pressure

A production process and low-pressure alcohol technology, which is applied in the field of medium and low-pressure alcohol and ether hydrazine production process, can solve the problems of low methanol synthesis rate, low efficiency of methanol synthesis unit, high energy consumption, etc., and achieve the effect of reducing compression power consumption

Inactive Publication Date: 2009-12-16
FUZHOU UNIV +1
View PDF2 Cites 13 Cited by
  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, practice shows that the combined alcohol process has obvious shortcomings. For example, (1) in order to adapt to the overall ammonia synthesis process, the methanol synthesis pressure in the combined alcohol process is generally set at 13-15 MPa, while the ideal operating pressure of methanol is 5-8 MPa
Obviously, high pressure operation means high energy consumption
(2) In the process flow adopted by the co-alcohol process, a large amount of synthetic ammonia raw material gas needs to pass through the methanol synthesis unit, which will undoubtedly lead to low efficiency and high energy consumption of the methanol synthesis unit, and its technical indicators such as space-time yield and energy consumption cannot be compared with Large Methanol Comparable
However, the synthesis rate of methanol under low pressure is low, and the amount of released gas is large, so its material consumption and energy consumption are not satisfactory.

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
  • Process for producing alcohol-ether hydrazine under medium/low-pressure
  • Process for producing alcohol-ether hydrazine under medium/low-pressure

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0034] Methanol hydrazine process using coal as raw material.

[0035] refer to figure 1 , the semi-water gas (conventional process) obtained from coal oxygen-enriched oxidation is sent to compression 2 after crude desulfurization, transformation, decarburization 1, and fine desulfurization. The recirculating gas will enter the gas preheater and exchange heat with the hot synthesis gas coming out of the bottom of the synthesis tower. It will be heated to 200-220°C. It will enter the ring gap of the catalyst frame from the bottom of the synthesis tower and radially enter the catalyst between the tubes from the circumferential direction. Layer, at 225-255°C, hydrogen reacts with carbon monoxide and carbon dioxide to produce methanol and water. After the reaction, the gas converges in the central gas collecting pipe (temperature is 230-280°C) and then exits the synthesis tower. The gas enters the shell side of the intermediate heat exchanger and exchanges heat with the gas enter...

Embodiment 2

[0039] Methanol hydrazine with natural gas as raw material.

[0040] refer to figure 2 , the desulfurized natural gas undergoes one-stage steam reforming and two-stage autothermal reforming in the reforming process, then enters "transformation" and "decarbonization 1" to adjust the hydrogen-carbon ratio and then compresses it to 7.0MPa, which is separated from the circulating gas oil The recycle gas will join into the methanol synthesis tower, the methanol synthesis pressure is 6.95MPa and the temperature is 266°C. The tail gas after the synthesis outlet gas is separated from the alcohol product enters the deep shift to convert the CO in it into H 2 and CO 2 , and then remove CO by "decarbonization 2" 2 , enter the PSA CO removal system to remove trace CO, add pure nitrogen from the oxygen production process, adjust the hydrogen-nitrogen ratio of the gas to 3:1, and then combine with the ammonia synthesis cycle gas after oil removal and send it to the ammonia synthesis tow...

Embodiment 3

[0044] This example is the same as Example 1, except that the synthetic methanol part is changed to adopt a fluidized bed process to synthesize dimethyl ether. The dimethyl ether synthesis catalyst used is a copper-based composite catalyst, the reaction temperature is 268° C., and the reaction pressure is 5.0 MPa. Part of the gas after separation of dimethyl ether enters the cycler as a cycle gas, and the other part is sent to the "deep shift" process to convert the CO contained in this part of the tail gas into H 2 and CO 2 , and then into decarburization 2, the contained CO 2 Removal, the residual trace CO in the secondary decarburization gas enters the PSA system and is completely removed. In this way, the purified gas is added with an appropriate amount of pure nitrogen from the nitrogen production process, and the hydrogen-nitrogen ratio of the gas is adjusted to 3, and then synthesized with ammonia. Meet and send to the ammonia synthesis tower, the ammonia synthesis pr...

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 provides a process for producing alcohol-ether hydrazine under medium / low-pressure, which solves the disadvantages of an alcohol-combining process in the prior art. A competitive replacement choice of the process is to serially connect alcohol-ether synthesis and ammonia synthesis into one production line, wherein alcohol-ether synthesis is performed first, and then ammonia synthesis is performed, but alcohol-ether synthesis and ammonia synthesis are relatively independent of the separation of respective products thereof; different proportion and the yield proportion of two products are flexible to regulate; ammonia synthesis does not need the process of additionally adding synthesis gas for compression; and the total pressure is 4 to 15 MPa. The process has the advantages of effectively reducing the power consumption of compression, realizing the flexible proportion regulation of alcohol or ether products, improving the efficiency of the whole technological process, reducing production cost to the utmost extent and laying a foundation for technical progress of the coal chemical industry and large-scale comprehensive development.

Description

technical field [0001] The invention belongs to the technical field of synthesis alcohol, ether and ammonia synthesis, and more specifically relates to a production process of medium and low pressure alcohol and ether hydrazine. Background technique [0002] Synthetic ammonia co-production methanol process is a pioneering work in my country's chemical fertilizer industry, which not only makes new progress in energy saving and consumption reduction of synthetic ammonia, but also adjusts the product structure of chemical fertilizer enterprises, breaks through the situation of a single product, and strengthens the market of enterprises Resilience. But the practice shows that the alcohol-linked process has obvious disadvantages, for example, (1) In order to adapt to the overall ammonia synthesis process, the methanol synthesis pressure in the alcohol-linked process is generally set at 13-15MPa, while the ideal operating pressure of methanol is 5-8MPa. Obviously, high pressure op...

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 Applications(China)
IPC IPC(8): C07C27/20C07C29/16C07C41/01C07C31/04C07C43/04C01C1/04
Inventor 王榕魏可镁林建新倪军林炳裕莫崇望瞿胜
Owner FUZHOU UNIV
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