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A method for determining the process execution sequence in hydrogen network hydrogen saving

A technique for executing the sequence and determining the process, applied in the field of hydrogen network, can solve the problem of not being able to give the target of hydrogen consumption, and achieve the effect of simple design steps, small amount of calculation, and simple method

Active Publication Date: 2021-05-14
CANGZHOU NORMAL UNIV
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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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  • A method for determining the process execution sequence in hydrogen network hydrogen saving
  • A method for determining the process execution sequence in hydrogen network hydrogen saving
  • A method for determining the process execution sequence in hydrogen network hydrogen saving

Examples

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example

[0126] 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

[0127] Example 1, it is known that the hydrogen recovery rate HR=95%, and the impurity removal rate IR=95%.

[0128] After determining the execution sequence of the process, each process is also satisfied, that is, the first iteration is completed. Because the amount of the unused source stream in the first iteration is 209.37 mol·s-1, the purified source stream is 175.38 mol·s-1. The consumption of the source stream after purification is 182.40 mol·s-1. Because 175.38<182.40, 175.38 is used as the initial value of the next iteration, and the final design is obtained after four iterations. The results of each iteration are shown in Table 3.

[0129] Table 3. Iterative Design Results of Example 1

[0130]

[0131] see final design Figure 4 , the amount of the external source stream designed is 41.53mol·s-1, the amount of 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 concentrat...

example 2

[0132] Example 2, the impurity concentration of the purified source stream is Creg=(0.03, 0.25, 0.72) mol%, and the hydrogen recovery rate is HR=95%.

[0133] The proposed method is used in the following design.

[0134] The method of satisfying the process from the source stream and the method of judging the execution sequence of the process are the same as above, and the design steps are similar to the above. Because the amount of the source stream that was not reused in the first iteration was 192.60 mol·s-1, the amount of the source stream after purification was 160.91 mol·s-1. The consumption amount of the source stream after purification is 200.47mol·s-1. Because 160.91<200.47, the amount of 160.91mol·s-1 of the source stream after purification obtained from the purification of the source stream before purification with an amount of 192.60mol·s-1 is not enough, and it is used as the initial value of the next iteration, The final design was obtained after six iterations...

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Abstract

The invention belongs to the field of hydrogen network technology, and discloses a new method for determining the execution order of processes in the hydrogen saving of hydrogen networks. First, the current source streams are used to satisfy each unexecuted process respectively by using the source stream distribution method, and sequentially according to the amount of external source streams or The principle that the process with the largest amount of source stream consumption after purification is executed first is used to determine the execution order of the process; the determined process execution order is combined with the iterative method of designing a fixed hydrogen concentration model after purification and a hydrogen network with a given impurity removal rate model, and respectively design Two models of multi-impurity hydrogen networks. The design method of the present invention can minimize the consumption of external source streams. For the former model, the consumption of external source streams, the consumption of source streams after purification and the discharge of fuel gas have been reduced by 1.60%, 3.71% and 2.00% respectively; for the latter model For this model, the reductions were 4.05%, 0.43%, and 4.94%, respectively, in the case of slightly lower impurity concentrations in the source stream after purification.

Description

technical field [0001] The invention belongs to the technical field of hydrogen networks, and in particular relates to a method for determining the execution order of processes in the hydrogen saving of hydrogen networks. Background technique [0002] Hydrogen has become a very important resource at present. A large amount of hydrogen is needed in the hydrogenation process of petroleum refining and chemical enterprises. With the heavy and inferior quality 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 consumption, hydrogen production, and hydrogen purification units, and there are close connections between these devices, the above-mentioned devices are often regarded as a hydrogen network. [0003] Compared with the hydrogen network that only considers reuse, schol...

Claims

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Application Information

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Patent Type & Authority Patents(China)
IPC IPC(8): G06Q10/08G06Q10/06
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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