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Novel hydrogen peroxide multistage catalytic decomposition type gas generator

A technology of gas generator and hydrogen peroxide, applied in chemical/physical/physicochemical fixed reactors, chemical instruments and methods, chemical/physical processes, etc., can solve the problem of pressure oscillation at the inlet and outlet of the generator, and temperature at the outlet of the generator Problems such as lowering and reducing the working efficiency of the generator, to achieve the effect of matching pressure drop, suppressing pressure oscillation, ensuring structural stability and flow resistance characteristics

Active Publication Date: 2021-11-19
合肥中科重明科技有限公司 +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0003] However, due to the influence of factors such as the bed load of the catalytic bed and the gas-liquid two-phase flow in the reaction chamber, the flow adjustment range of this type of generator is limited; specifically, during use, when the actual flow is less than the design flow, It is easy to cause pressure oscillation at the inlet and outlet of the generator ( figure 1 As shown), thus affecting the normal use; when the actual flow rate exceeds the design value, due to the insufficient reaction of part of the hydrogen peroxide, the outlet temperature of the generator will drop, reducing the working efficiency of the generator

Method used

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  • Novel hydrogen peroxide multistage catalytic decomposition type gas generator
  • Novel hydrogen peroxide multistage catalytic decomposition type gas generator
  • Novel hydrogen peroxide multistage catalytic decomposition type gas generator

Examples

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Embodiment 1

[0032] In this embodiment, as shown in Figure 2-4, a novel hydrogen peroxide multi-stage catalytic decomposition gas generator includes a first-stage hydrogen peroxide inlet 1, and the downstream of the first-stage hydrogen peroxide inlet 1 is sequentially provided with 1 Two-stage hydrogen peroxide silver mesh catalytic bed, one-stage lattice structure 3, two-stage hydrogen peroxide gas-liquid injection plate 7, two-stage downstream mixing chamber 10, two-stage lattice structure 4, three-stage hydrogen peroxide gas-liquid injection Injection disk 9, 3rd stage downstream mixing chamber 11, 3rd stage lattice structure 5 and generator outlet 12, 2nd stage hydrogen peroxide gas-liquid injection disk 7 is provided with 2nd stage hydrogen peroxide inlet 6, 3rd stage hydrogen peroxide gas A three-stage hydrogen peroxide inlet 8 is provided on the liquid injection plate 9 . The casing of the gas generator, the first-level lattice structure 3, the second-level lattice structure 4, the...

Embodiment 2

[0035] On the basis of embodiment 1, the using method of this novel hydrogen peroxide multistage catalytic decomposition type gas generator is as follows:

[0036] S1: Hydrogen peroxide enters the first-level hydrogen peroxide silver mesh catalyst bed 2 through the first-level hydrogen peroxide inlet 1, and after rectification and distribution, it is decomposed into high-temperature oxygen and water vapor and flows into the first-level lattice structure 3; in this step The time of hydrogen peroxide feeding is sufficient to fully activate the silver screen. When the gas at the outlet 12 of the generator is observed to change from white mist to transparent or when the temperature of the decomposed gas reaches the decomposition temperature, the hydrogen peroxide inlet 6 of the second stage can be passed through. into hydrogen peroxide;

[0037] S2: When the temperature of the decomposed gas at the outlet 12 of the monitoring generator reaches the decomposition temperature, hydrog...

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Abstract

The invention relates to the field of rocket engines, in particular to a novel hydrogen peroxide multistage catalytic decomposition type gas generator, which comprises a first-stage hydrogen peroxide inlet, wherein a first-stage hydrogen peroxide silver mesh catalytic bed, a first-stage lattice structure, a second-stage hydrogen peroxide gas-liquid injection disc, a second-stage downstream mixing cavity, a second-stage lattice structure, a third-stage hydrogen peroxide gas-liquid injection disc, a third-stage downstream mixing cavity, a third-stage lattice structure and a generator outlet are sequentially arranged on the downstream of the first-stage hydrogen peroxide inlet, a second-stage hydrogen peroxide inlet is formed in the second-stage hydrogen peroxide gas-liquid injection disc, and a third-stage hydrogen peroxide inlet is formed in the third-stage hydrogen peroxide gas-liquid injection disc. According to the gas generator, high-temperature and high-pressure gas with rated flow is generated through self-decomposition reaction of multistage hydrogen peroxide, mechanical equipment such as a turbine and the like are pushed to do work, large-range adjustment of the flow of the gas generator is achieved through three-stage gas inlet, it is guaranteed that the working pressure is stable, and the power capability of the generator is improved.

Description

technical field [0001] The invention relates to the technical field of rocket engines, in particular to a novel hydrogen peroxide multistage catalytic decomposition gas generator. Background technique [0002] In recent years, reusable rockets have become a development hotspot and trend in aerospace at home and abroad, which can greatly reduce the cost of space launches. The engine system of the rocket is the core of the rocket, and the gas generator cycle is one of the main cycle modes of the rocket engine. Commonly used generators for rockets are divided into oil-rich gas generators and oxygen-rich gas generators. Oxygen-enriched combustion can make full use of fuel. If the concentration of oxygen can be controlled, it can effectively control the burning of oxygen-enriched components such as the combustion chamber, thereby improving the working efficiency and service life of the generator. The method of directly driving the turbine to do work through the catalytic reacti...

Claims

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Application Information

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IPC IPC(8): B01J19/24B01J19/00B01J4/00
CPCB01J19/24B01J19/0053B01J19/0006B01J4/002B01J19/0013B01J2204/002B01J2219/00063
Inventor 张大尉张泰昌袁杨青鲁碧为范学军
Owner 合肥中科重明科技有限公司
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