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New method for determining process execution sequence in hydrogen network node hydrogen

A technology that executes the sequence and determines the process, applied in the field of hydrogen network, can solve the problem that the target of hydrogen consumption cannot be given

Active Publication Date: 2017-07-18
CANGZHOU NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

However, this qualitative conclusion cannot give a hydrogen consumption target; Liu et al. proposed a hydrogen network purification unit model to evaluate the feasibility of the purification scheme; Agrawal et al. proposed a diagram that does not require iteration based on the concept of the limit composite curve method, by constructing a limiting hydrogen distribution diagram to discuss the hydrogen network with purification units, and give a method to calculate the target value of hydrogen consumption; Foo et al. proposed a method called gas cascade analysis (GCA) to calculate the available Hydrogen target, and discussed the situation with two purification units; Ng et al. proposed an automation-based target pinch technology for the design of reuse hydrogen network, and Ng et al. improved it to study the purification problem of hydrogen stream ; Zhang et al. proposed a graphical method to obtain the pinch concentration and hydrogen consumption target of the hydrogen network of the purification unit through the impurity load-flow rate composite curve

Method used

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  • New method for determining process execution sequence in hydrogen network node hydrogen
  • New method for determining process execution sequence in hydrogen network node hydrogen
  • New method for determining process execution sequence in hydrogen network node hydrogen

Examples

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example

[0124] The above example is designed according to the fixed concentration model after purification (HR=95%, Creg=(0.03,0.25,0.72)mol%) and the given impurity removal rate model (HR=95%, R=95%).

example 1

[0125] Example 1, it is known that the hydrogen recovery rate is HR=95%, and the impurity removal rate IR=95%.

[0126] After determining the order of process execution, all processes are also satisfied, that is, the first iteration is completed. Because the amount of the last recycled source stream in the first iteration is 209.37 mol·s-1, the purified source stream is 175.38 mol·s-1 after purification. The amount of source stream after purification is 182.40 mol·s-1. Because of 175.38 <182.40, so use 175.38 as the initial value of the next iteration, and get the final design after four iterations. The results of each iteration are shown in Table 3.

[0127] Table 3. Iterative design results of Case 1

[0128]

[0129] See you in the final design Figure 4 , The designed external source stream consumption is 41.53mol·s-1, the source stream after purification is 172.89mol·s-1, the amount of the source stream before purification is 206.55mol·s-1, and the impurity concentration after...

example 2

[0130] Example 2: The impurity concentration of the source stream after purification is Creg=(0.03, 0.25, 0.72) mol%, and the hydrogen recovery rate is HR=95%.

[0131] Use the proposed method to design below.

[0132] The method of satisfying the process by the source logistics and the method of judging the execution order of the process are the same as above, and the design steps are similar to the above. Because the amount of the last recycled source stream in the first iteration is 192.60 mol·s-1, the amount of the source stream after its purification is 160.91 mol·s-1. The amount of source stream after purification is 200.47 mol·s-1. Because of 160.91 <200.47, so the amount of 160.91mol·s-1 of the purified source stream obtained from the purification of the source stream before the purification with the amount of 192.60mol·s-1 is not enough. Use it as the initial value of the next iteration and The final design is obtained in six iterations, and the results of each iteration...

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Abstract

The invention belongs to the technical field of the hydrogen network, and discloses a new method for determining a process execution sequence in hydrogen network node hydrogen. The new method comprises the following steps that: firstly, applying a source logistics distribution method to enable current source logistics to independently meet each process which is not executed, and determining a process execution sequence according to a principle that a process with a maximum external source logistics use amount or purified source logistics use amount in sequence; combining the determined process execution sequence with an iteration method for designing a fixed purified hydrogen concentration model and a given impurity removal rate model hydrogen network to independently design the multiple-impurity hydrogen network of two types of models. By use of the design method disclosed by the invention, the external source logistics use amount is minimized. For a previous model, the external source logistics use amount, the purified source logistics use amount and a fuel gas discharge value are independently reduced by 1.60%, 3.71% and 2.00%. For a last model, under a situation that the purified source logistics impurity concentration is low, the external source logistics use amount, the purified source logistics use amount and a fuel gas discharge value are independently reduced by 4.05%, 0.43% and 4.94%.

Description

Technical field [0001] The invention belongs to the technical field of hydrogen networks, and in particular relates to a new method for determining the execution sequence of processes in the hydrogen saving of hydrogen networks. Background technique [0002] Hydrogen has now become a very important resource. A large amount of hydrogen is used in the hydrogenation process of petroleum refining and chemical enterprises. With the heavyization and deterioration of crude oil and the implementation of increasingly stringent industrial environmental protection standards and related legislation, the demand for hydrogen in the hydrogenation process continues to increase . When there are multiple devices such as hydrogen consuming, hydrogen production, and hydrogen purification units, and there are close connections between these devices, these devices are often regarded as hydrogen networks. [0003] Compared with hydrogen networks that only consider recycling, scholars from various count...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): G06F17/50
CPCG06F30/18
Inventor 王焕云潘春晖潘文博马力常炳双辛健周自成
Owner CANGZHOU NORMAL UNIV
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