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Variation of ammonia ratio in Andrussow process

A proportional, hydrogen cyanide technology, applied in the preparation/purification/separation, liquefaction, cyanide and other directions of hydrogen cyanide, can solve problems such as high variable costs, and achieve the effect of reducing costs and improving variable costs

Active Publication Date: 2014-06-18
INVISTA TEXTILES (U K) LTD
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0012] The problem of high and variable costs for HCN production is solved or ameliorated by operating the HCN reaction at adjusted (e.g., atypical) ammonia:methane ratios based on natural gas (e.g., methane) and ammonia prices

Method used

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  • Variation of ammonia ratio in Andrussow process
  • Variation of ammonia ratio in Andrussow process

Examples

Experimental program
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Embodiment 1

[0076] Embodiment 1: change methane: ammonia molar ratio

[0077] Filtered ammonia, natural gas, and air or oxygen are fed into an Andrussow reactor and heated at a temperature in the range of about 1,050°C to about 1,200°C in the presence of a platinum-containing catalyst. A 4 inch inner diameter stainless steel reactor with a ceramic insulating liner inside was used for the pilot test. Forty pieces of 90 wt% Pt / 10 wt% Rh 40 mesh gauze from Johnson Matthey (USA) were loaded as catalyst bed. A perforated alumina sheet was used for the catalyst sheet support. Set the total flow rate at 2532 SCFH (standard cubic feet per hour). Some reactors are designed to use air as the oxygen source. Other Andrussow reactor designs use oxygen-enriched air and still others use oxygen as the oxygen-containing feed stream. However, the ratio of ammonia to methane can be varied in any of these methods to reduce cost. Natural gas can also be used instead of pure methane, especially if the nat...

Embodiment 2

[0091] Example 2: Impurity formation when unused methane is present

[0092] The Andrussow process was performed as described in Example 1, except that the amount of methane in the reaction vessel was varied. When the amount of methane in the reaction vessel increases beyond the level at which the methane is substantially consumed, some methane remains unreacted and exits through the reaction vessel. This unreacted methane is detected in the product stream and is referred to as "methane slip" or "methane loss".

[0093] Such as Figure 4 As shown in , the acetonitrile (CH 3 CN) The amount of impurities increases with the amount of methane leakage (unreacted methane). especially, Figure 4 Illustratively, when unreacted methane is greater than about 0.5 mole % methane per mole of HCN produced, significant amounts of acetonitrile begin to form, and increasing amounts of acetonitrile continue to form as the amount of unreacted methane increases.

[0094] During typical opera...

Embodiment 3

[0095] Embodiment 3: Use cost to change the molar ratio of methane and ammonia

[0096] This example illustrates the realization of cost savings for HCN production after evaluation of ammonia and methane costs and using this evaluation to adjust the methane:ammonia ratio in the Andrussow process.

[0097] The oxygen Andrussow process was performed as described in Example 1, but with a methane:ammonia ratio of about 0.8.

[0098] The average total percentage cost of methane for one week is X and the average total percentage cost of ammonia for the same week is Y. The cost of ammonia and methane is 90% of the total operating cost for the production of HCN (X+Y=90% of the total cost).

[0099] Since the methane:ammonia ratio is about 0.8, about 20% less methane than ammonia is used in this reaction. Thus, if the cost per mole of methane is about 0.01 of the cost per mole of ammonia, the total methane cost (X) is 0.008 of the total ammonia cost (Y), and X=0.008(Y) or Y=X / 0.008. ...

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Abstract

The invention discloses variation of ammonia ratio in an Andrussow process. Methane and ammonia raw materials are typically the major costs for HCN production. The methods described herein can be used to vary the molar ratio of methane to ammonia during HCN production to reduce costs.

Description

[0001] Cross References to Related Applications [0002] This application claims priority to U.S. Provisional Patent Application Serial No. 61 / 738,727, entitled "VARIATION OF AMMONIA RATIO IN ANDRUSSOW PROCESS," filed December 18, 2012, which The disclosure is hereby incorporated by reference in its entirety. technical field [0003] The present disclosure relates to varying the feed composition to an Andrussow process for the production of hydrogen cyanide (HCN) from methane, ammonia and oxygen. Background technique [0004] The Andrussow process converts ammonia and methane gases into hydrogen cyanide (HCN) in the presence of oxygen and a platinum catalyst. The response is as follows: [0005] 2NH 3 +2CH 4 +3O 2 →2HCN+6H 2 o [0006] Ammonia (NH 3 ), methane (CH 4 ) and an oxygen source (eg, air) are fed into the reactor and heated to a temperature of up to about 2,500° C. in the presence of a platinum or platinum alloy catalyst. [0007] The availability and pri...

Claims

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Application Information

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IPC IPC(8): C01C3/02
CPCC01C3/0212F25J3/0228B01D53/00
Inventor 斯图尔特·福赛思刘爱国马丁·J·伦纳布伦特·J·斯塔尔曼
Owner INVISTA TEXTILES (U K) LTD
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