Combined purifying technique for ammonia preparation from natural gas, ammonia preparation from coal and methanol preparation from coal

A technology of coal-to-methanol and purification process, which is applied in the field of synthesis gas purification of natural gas to ammonia, coal to ammonia and coal to methanol, and to purification of synthesis gas from natural gas and coal to gas, which can solve the difficulty of operation and high control requirements, increasing Coal-to-ammonia gas purification process design and operation control are difficult, purification energy consumption is large, etc., to achieve the effect of reducing the number of washing stages and trays, eliminating the cooling equipment between stages, and reducing investment

Inactive Publication Date: 2010-06-02
罗庆洪
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0005] 2. The energy consumption of raw process gas purification of coal-to-ammonia is relatively large:
[0009] 4. The low-temperature methanol purification process of coal-to-ammonia raw process gas is difficult to operate and requires high control:
[0010] In the coal-to-ammonia process, since the outlet of the coal-to-ammonia raw process gas scrubber must be strictly controlled to a very low CO 2 content, thus greatly increasing the difficulty of the design and operation control of the coal-to-ammonia gas purification process, so as to meet the CO 2 strict requirements

Method used

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  • Combined purifying technique for ammonia preparation from natural gas, ammonia preparation from coal and methanol preparation from coal
  • Combined purifying technique for ammonia preparation from natural gas, ammonia preparation from coal and methanol preparation from coal
  • Combined purifying technique for ammonia preparation from natural gas, ammonia preparation from coal and methanol preparation from coal

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Effect test

Embodiment 1

[0038] The inventor has obtained through research: the three independent processes of natural gas ammonia production process, coal ammonia production process, and coal methanol process will be combined into multi-raw material polygeneration process, and the key technology is to carry out the purification process part that the three processes all have. Comprehensive configuration to realize the optimized combined purification process, the optimized combined purification process is as follows:

[0039] The combined purification process of natural gas ammonia production and coal ammonia production and coal methanol production process of the present invention utilizes the CO removal in the purification system in the existing natural gas ammonia production process 2 purification device. In the low-temperature methanol purification system for coal-to-methanol and coal-to-ammonia process gas, the partially converted coal-to-methanol process gas from coal-to-methanol process gas is pa...

Embodiment 2

[0043] On the basis of optimizing the combined purification process in Example 1, the H discharged from the coal-to-methanol process gas scrubber 2 +CO+CO 2 The methanol synthesis gas is fed into the follow-up process and the methanol synthesis tower to prepare methanol; the coal-to-methanol process gas scrubber and the coal-to-ammonia process gas scrubber respectively discharge methanol-rich liquid, which is sulfur-containing methanol-rich liquid, containing Sulfur-methanol-rich liquid needs to be regenerated in the follow-up system to recover sulfur; after the semi-lean liquid is taken out from the coal-to-methanol process gas scrubber (CO2 has been absorbed 2 , can also absorb CO 2 methanol solution), and the semi-lean liquid is removed from the gas phase CO in the flash tank and then passed to the top of the coal-to-ammonia process gas scrubber to wash the coal-to-ammonia process gas.

[0044] When the two processes of natural gas ammonia production and coal ammonia prod...

Embodiment 3

[0046] On the basis of embodiment 2 optimization combined purification process, only two kinds of gas ratios of the following two items are preferred:

[0047] It is preferable to use the coal-to-ammonia process gas scrubber to remove the H used for ammonia synthesis 2 +CO 2 H in the mixed gas 2 The weight is enough to meet all the H consumed by the existing natural gas ammonia plant 2 50% to 80% of the weight to determine the H used for ammonia synthesis in the gas scrubber of the coal-to-ammonia process 2 +CO 2 The weight of the mixed gas; the H used for ammonia synthesis is taken out from the gas scrubber of the coal-to-ammonia process 2 +CO 2 H in the mixed gas 2 with CO 2 The weight ratio is 0.13~0.15:1.

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Abstract

The combined purification process of ammonia preparation with natural gas and coal as well as methanol preparation with coal belongs to the purification technical field of synthesis gas of ammonia preparation with natural gas and coal as well as methanol preparation with coal. In the low-temperature methanol purification system of the process gas of methanol preparation with coal and ammonia withcoal, the coal gas is fed into the bottom of the coal prepared methanol and coal prepared ammonia process gas scrubber; meanwhile, fresh methanol solution with the temperature of about 64 DEG C belowzero is used to wash only the coal prepared methanol process gas; the semi lean solution is taken out of the coal prepared ammonia process gas scrubber to wash the coal prepared ammonia process gas; the H2+CO2 mixed gas used for synthesising ammonia is taken out from the coal prepared ammonia process gas scrubber and fed in the CO2 purification device of the prior natural gas prepared ammonia process purification system; the follow-up process of the prior natural gas prepared ammonia is used to prepare ammonia. The invention has the advantages of the optimization and the combination of three independent processes, namely ammonia preparation with natural gas, ammonia preparation with coal and methanol preparation with coal, system simplification, energy consumption saving, and reduction ofequipment quantity and investment.

Description

technical field [0001] The invention belongs to the technical field of synthesis gas purification from natural gas and coal gas, in particular to the technical field of synthesis gas purification for ammonia production from natural gas, ammonia from coal and methanol from coal. Background technique [0002] The existing natural gas ammonia production and coal gas ammonia production are two completely independent processes, using two sets of equipment respectively, and coal gas production has the technical ability to simultaneously provide raw material gas to methanol production equipment and synthetic ammonia production equipment. However, the intermediate substances used for ammonia production after desulfurization and purification of natural gas ammonia and coal gas are basically the same, which makes the two sets of ammonia production processes and equipment flow duplication after desulfurization and purification, large investment and relatively large energy consumption. ...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): C01B3/50C01B3/52C10K1/00C10K1/08
Inventor 罗庆洪
Owner 罗庆洪
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