Energy-saving urea production system and production process thereof

A production system, energy-saving technology, applied in the chemical industry, preparation of urea derivatives, sustainable manufacturing/processing, etc., can solve the problems of poor heat classification and utilization, uneven distribution of reaction heat, and high investment.

Active Publication Date: 2015-08-12
SICHUAN GOLDEN ELEPHANT SINCERITY CHEM CO LTD
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  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0014] However, the production process of the aqueous solution full circulation method in the above-mentioned prior art still has the following technical defects: first, the common urea synthesis tower of the existing aqueous solution full circulation process generally has the following problems: uneven mixing of materials, uneven distribution of reaction heat, and partial urea synthesis rate. Low' and other defects
However, to design a urea synthesis high-pressure ring, the technical difficulty of equipment design and manufacture is very high, and the investment is also expensive, which makes it difficult to increase the conversion rate of urea synthesis to about 73%.
[0015] Second, the consumption of products is higher
Due to the low conversion rate of the aqueous solution full circulation method, there are many materials that need to be heated and decomposed, resulting in high steam consumption. Therefore, the steam consumption of this process is relatively high. Generally, the steam consumption per ton of urea is about 1100kg.
At the same time, because the decomposed materials need to be recycled, the consumption of circulating cooling water is increased. Generally, the consumption of circulating cooling water per ton of urea is 140M 3
[0016] Third, the graded utilization of heat is poor
Although the domestic improved full circulation method of aqueous solution has high energy consumption, the investment is relatively low. Therefore, it is urgent to develop a urea production process with low investment and low energy consumption, which can reach the international advanced level.

Method used

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  • Energy-saving urea production system and production process thereof
  • Energy-saving urea production system and production process thereof

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Embodiment 1

[0066] The energy-saving full-cycle urea production system described in this embodiment is as figure 2 As shown, the system includes: CO 2 Compressor, carbamate pump (short for ammonium carbamate pump), liquid ammonia pump and urea synthesis tower, CO 2 The compressors are respectively connected with a carbamate pump and a liquid ammonia pump, and the liquid ammonia pump is connected with a urea synthesis tower. After the urea synthesis tower, a falling film countercurrent medium pressure decomposition tower and a heater, a carbamate condenser, and a carbamate are sequentially connected in series. Separator, three-stage medium pressure absorption tower and evaporative ammonia cold recovery device, liquid ammonia buffer tank, inert gas scrubber, tail gas ammonia cleaning device, low pressure decomposition tower and heater, dimethyl liquid preheater, horizontal Low-pressure absorber, falling film pre-evaporator, one-stage evaporator and one-stage evaporative condenser, two-stage ...

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Abstract

The invention belongs to the field of urea preparation, and particularly relates to an energy-saving urea production system and a production process thereof. The system comprises a CO2 compressor, an ammonium carbamate pump, a liquid ammonia pump and a urea synthesizer. The system is characterized in that the CO2 compressor is connected with the ammonium carbamate pump and the liquid ammonia pump, the liquid ammonia pump is connected with the urea synthesizer, a falling-film countercurrent medium-pressure decomposing tower and a heater, an ammonium carbamate condenser, an ammonium carbamate separator, a three-stage medium-pressure absorption tower and an evaporative ammonia refrigeration recoverer, a liquid ammonia buffer tank, an inert gas scrubber, a tail-gas ammonia cleaning fine purifier, a low-pressure decomposing tower and a heater, a dimethyl liquid preheater, a horizontal low-pressure absorber, a falling film type pre-evaporator, a one-stage evaporator and a one-stage evaporative condenser, a two-stage evaporator and a two-stage evaporative condenser, and a process wastewater desorption and hydrolysis tower are sequentially connected behind the urea synthesizer in sequence. The energy-saving urea production system has the advantages of low investment, low energy consumption, simple operation, high elasticity and the like, thereby the process technology has considerable economic benefit and social benefit.

Description

Technical field [0001] The invention belongs to the field of urea preparation, and is specifically an energy-saving urea production system and a production process thereof. Background technique [0002] Urea【CO(NH 2 ) 2 】Alternatives are carbamide, carbamide, urea, which mainly exist in the urine excreted by humans and animals in nature. It has a wide range of uses, not only a high-efficiency nitrogen fertilizer used in agricultural production, but also a common chemical raw material in industry. [0003] In 1773, the chemist Rouelle first discovered urea while evaporating urine. It was identified as a new substance by FoUrcray and Vauqudin in 1798 and named it urea. In 1828, Uvohler produced urea while heating ammonium cyanate in the laboratory. The reaction was: Nl{4CN0=NH2c∞m2. In 1886, Bassroff's first successful experiment was adopted by modern industry. A method of directly synthesizing urea from ammonia and carbon dioxide. [0004] In 1922, Germany first used ammonia and c...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C273/04
CPCY02P20/10
Inventor 李旭初刘朝慧雷林刘胜赵树良方一
Owner SICHUAN GOLDEN ELEPHANT SINCERITY CHEM CO LTD
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