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Continuous production method of granular humic acid urea and activation reactor

A technology of humic acid urea and a production method, which is applied in the field of agricultural fertilizer production, can solve the problems that the nitrogen utilization efficiency in urea cannot be effectively improved, the best reaction effect of humic acid urea is affected, and it is not suitable for large-scale production and application, and the activation reaction is achieved. Short time, saving reaction time, the effect of short reaction time

Active Publication Date: 2013-09-25
INST OF AGRI RESOURCES & ENVIRONMENT SHANDONG ACADEMY OF AGRI SCI +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

This method uses molten urea, and its limitation is that the production must be connected with the urea production process. If this method is used in areas far away from urea production plants, the energy consumption will be too high and it is not suitable for large-scale production.
Chinese patents CN102153424A, CN1169975A, CN102260111A, and CN102249814A disclose the reaction conditions of the complexation of urea and humic acid and the process of producing fertilizers. The method adopted in these patents is to perform solid-liquid separation after the two fully react and then add or not add other raw materials Made into fertilizer, it is not suitable for large-scale production and application due to the high energy consumption of the solid-liquid separation process
Chinese patents CN1887819A and CN1580005A disclose the method of making fertilizer with urea and humic acid. The method of these two patents is to directly mix the two, and then add other raw materials to granulate. There is no reaction between the two, which is a simple mixed fertilizer process. Among them, the effect of humic acid is difficult to exert, and it cannot effectively improve the utilization efficiency of nitrogen in urea
The equipment uses steam heating, which is difficult to achieve stable temperature control, which affects the best reaction effect of humic acid urea. Two screw propellers are used, and the production efficiency is low.

Method used

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  • Continuous production method of granular humic acid urea and activation reactor
  • Continuous production method of granular humic acid urea and activation reactor
  • Continuous production method of granular humic acid urea and activation reactor

Examples

Experimental program
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Effect test

Embodiment 1

[0052] An activation reactor with a structure such as figure 1 , figure 2 , image 3 Shown, comprise airtight horizontal tank body and motor, airtight horizontal tank body is arranged on the base bracket 10, horizontal tank body comprises inner tank body and outer tank body 2, and the space between inner tank body and outer tank body The cavity is a heat transfer jacket, and the heat transfer jacket is filled with heat-conducting oil. On the side wall of the outer tank body 2, an oil inlet 3 and an oil outlet 4 are connected to the heat transfer jacket. On the side wall of the outer tank body 2 It is also provided with a feed port 6 and a discharge port 7 respectively connected to the inside of the inner tank body, and three stirring shafts 1 are arranged in the inner tank body. The stirring shaft 1 is driven by a motor, and the side wall of each stirring shaft 1 is There are two inner and outer layers, and the cavity between the inner and outer side walls is a heat transfe...

Embodiment 2

[0056] A kind of activation reactor, structure is shown in embodiment 1, difference is:

[0057] The feed port 6 is set on the upper part of the outer tank body 2, the discharge port 7 is set on the lower part of the outer tank body 2, the horizontal distance between the feed port 6 and the discharge port 7 is 4200 mm, and the oil inlet 3 is located at the lower part of the outer tank body 2 , the oil outlet 4 is located on the upper part of the outer tank body 2, and the horizontal distance between the oil inlet 3 and the oil outlet 4 is 4300mm.

[0058] The three stirring shafts 1 are arranged in an equilateral triangle in the inner tank, and the distance between two adjacent stirring shafts is 250mm. The diameter of the outer ring of the spiral blade is 260 mm. The minimum distance between the outer edge of the spiral blade on each stirring shaft and the inner tank is 120mm.

[0059] The airtight horizontal tank is 4500mm long, the inner diameter of the inner tank is 920m...

Embodiment 3

[0061] A continuous production method of granular humic acid urea, comprising using the activation reactor described in embodiment 1, the steps are as follows:

[0062] (1) Preparation of liquid catalyst

[0063] The raw materials are composed as follows in parts by weight: 20 parts of potassium hydroxide and 80 parts of water. Dissolve potassium hydroxide in water to prepare a potassium hydroxide solution.

[0064] (2) Preparation of mixed materials

[0065] Pulverize the lignite through a pulverizer, pass through a 150-mesh sieve, transport the sieved lignite, granular urea, and ammonium bicarbonate powder to a material mixer for full stirring and mixing, then spray potassium hydroxide solution, and immediately stir and mix evenly to obtain The mixed material is composed as follows in parts by weight: 33 parts of lignite, 57 parts of urea, 6 parts of ammonium bicarbonate powder, and 4 parts of potassium hydroxide solution.

[0066] (3) Turn on the activation reactor, pass...

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Abstract

The invention relates to a continuous production method of granular humic acid urea and an activation reactor. The method comprises the following steps of: mixing granular urea and decomposed coal or brown coal with a catalyst; performing activation reaction on the mixture in the activation reactor; and cooling, crushing and prilling to prepare the granular humic acid urea fertilizer. A heat transfer jacket is arranged between an inner tank body and an outer tank body of the activation reactor. The tank body is internally provided with three stirring shafts. Interlayers are arranged on the side walls of the stirring shafts. Each spiral blade is internally of a hollow structure. Heat transfer oil is filled in the heat transfer jacket, the heat transfer interlayers and the hollow structures of the spiral blades. According to the invention, the process is short in reaction time, the activation reactor is heated adequately and uniformly, and urea is not crushed or melted, so that the energy consumption of whole production is greatly reduced.

Description

technical field [0001] The invention relates to a method for continuously producing granular humic acid urea by reacting weathered coal or lignite with urea, and belongs to the technical field of agricultural fertilizer production. Background technique [0002] my country is a big country in the use of fertilizers, and urea is one of the most important nitrogen fertilizers. The annual output of urea is about 55 million tons, and the domestic use is about 43 million tons. However, the utilization rate of urea in farmland is low, only 30%-35%. Part of nitrogen volatilizes in the form of ammonia and nitrous oxide or leaches into groundwater in the form of nitrate, causing environmental pollution and waste of resources. [0003] In order to improve the utilization efficiency of nitrogen in urea, scholars have conducted a lot of research and developed a variety of technical means and methods to improve the utilization efficiency of nitrogen in urea. Under certain conditions, ure...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C05G1/00
Inventor 李彦刘兆辉陈广思张英鹏张荣俊
Owner INST OF AGRI RESOURCES & ENVIRONMENT SHANDONG ACADEMY OF AGRI SCI
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