A process for nitric acid production

A nitric acid and process technology, which is applied in the production of bulk chemicals, hydrogen/synthesis gas production, chemical industry, etc., can solve the problems of excessive water vapor increase, high temperature, effective steam reforming, multiple The effect of heating

Pending Publication Date: 2020-12-22
CASALE SA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

In addition, steam generation increases with the efficiency of the nitric acid process and the ammonia process, since for these two processes higher efficiencies generally require lower water steam usage; therefore, increasing the efficiency of such processes is strongly discouraged , as this would only lead to an increase in excess water vapor

Method used

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  • A process for nitric acid production
  • A process for nitric acid production
  • A process for nitric acid production

Examples

Experimental program
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Effect test

Embodiment

[0105] refer to figure 1 , the advantages of the present invention will be better clarified by the following examples.

[0106] Reference is made to a nitric acid section 1 with a nitric acid production rate of 1500 t / day, where the temperature of the process gas 12 leaving the oxidation reactor 2 is 880°C and is cooled to 500°C. The steam reformer 104 of the ammonia section 100 is fed with a stream 110 having a steam to carbon ratio (S / C) of 3 at a temperature of 450° C. and a pressure of 25 bar. The ammonia consumption of nitric acid is 425 tons / day.

[0107] The nitric acid section 1 provides a steam reformer 104 with a load of 35 Gcal / h and allows obtaining a reformed gas 111 at a temperature of 800°C. Under these conditions, the ammonia production rate was 425 tons / day. From this it can be seen that figure 1 The plant produces enough ammonia to make nitric acid.

[0108] With regard to existing technologies for providing reforming heat by fuel combustion, according t...

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Abstract

Integrated process for the synthesis of ammonia and nitric acid including: a) production of an ammonia make-up synthesis gas,comprising steam reforming of a hydrocarbon feedstock under provision of steam reforming heat;catalytic conversion of said make-up synthesis gas into ammonia; catalytic oxidation of a stream of ammonia obtaining a process gas; absorption of said process gas with water obtaining nitric acid, wherein at least a portion of the steam reforming heat is recovered from said hot process gas.

Description

technical field [0001] The invention relates to the field of nitric acid production. Background technique [0002] Nitric acid is synthesized by the reaction of ammonia and oxygen. Specifically, one mole of nitric acid is obtained by reacting one mole of ammonia with two moles of oxygen according to the following reaction: [0003] NH 3 +2O 2 →HNO 3 +H 2 O (1) [0004] The synthesis of nitric acid mainly involves the catalytic oxidation of ammonia to produce nitrogen oxides including NOx (mainly NO and NO 2 ), N 2 A gas of O by-product, oxygen and nitrogen, and a subsequent step in which the gas is contacted with water, wherein the water and NO 2 react to produce nitric acid. The NO 2 The reaction with water to produce nitric acid is often called absorption. With NO 2 is absorbed, NO and O 2 The reaction produces more NO 2 . [0005] The absorption step usually also delivers N 2 O and residual NOx exhaust. The exhaust gas has a pressure above atmospheric pre...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C01C1/04C01B21/26C01B21/28
CPCC01B3/384C01B21/262C01B21/28C01B2203/0233C01B2203/0283C01B2203/043C01B2203/0475C01B2203/0816C01B2203/0833C01B2203/0866C01B2203/0894C01B2203/1241C01B2203/142C01C1/0488
Inventor 埃尔曼诺·菲力比拉斐尔·奥图尼弗朗西斯科·巴拉托
Owner CASALE SA
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