CN105032044A - Reaction environment control system in amino acid production process - Google Patents
Reaction environment control system in amino acid production process Download PDFInfo
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- CN105032044A CN105032044A CN201510247805.0A CN201510247805A CN105032044A CN 105032044 A CN105032044 A CN 105032044A CN 201510247805 A CN201510247805 A CN 201510247805A CN 105032044 A CN105032044 A CN 105032044A
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Abstract
The invention discloses a reaction environment control system in an amino acid production process. In the system, by means of centralized control on an air conditioning system, a vapor conditioning system, a self-cooling water source and a tap water source with advanced management method to achieve real-time adjustment on the conditions required water and gas in a reaction, strict control to each process step is achieved. The control system is simple in operation, can not only reduce personal cost in enterprises but also effectively increases production efficiency, and further reduce unnecessary consumption of materials. An air filter includes an air total filter and an air pre-filter which are same in structure, thereby increasing controllability of air filtration, so that more sensitive adjustment during monitoring of the reaction conditions of amino acids by operator is achieved. A check valve is connected between the A-stage filter and the air pre-filter in a series manner, so that air, which is filtered through the filters, is prevented from flowing back and further air parameters outputted by an output end are prevented from influences. The control system is more scientific and simple in design.
Description
Technical field
The present invention relates to amino acid preparation field, particularly relate to reaction environment control system in a seed amino acid processing procedure.
Background technology
Amino acid is the common name of the class organic compound containing amino and carboxyl.The basic composition unit of biological function macro-molecular protein is the base substance forming Animal nutrition desired protein.It is the organic compound containing a basic amine group and an acidic carboxypolymer.Amino be connected on α-carbon for a-amino acid.The amino acid of constitutive protein matter is a-amino acid.
Amino acid is pharmaceutically being mainly used to prepare Hausmam Amin 20, also as medicine with for the synthesis of polypeptide drugs.Amino acid as medicine has 100 kinds, has 20 kinds to have kind more than 100 with the amino acid forming nonprotein comprising the amino acid forming protein.The compound preparation be made up of several amino acids occupies very important status in modern PN solution and " essential food " therapy, to the nutrition maintaining urgent patient, rescue patient vitals to have a positive effect, become one of medical kind indispensable in modern medical service.The amino acid independent role such as glutamic acid, arginine, asparatate, cystine, L-3,4 dihydroxyphenylalanine treatment some diseases, is mainly used in treatment hepatopathy disease, disease of digestive tract, encephalopathic, cardiovascular disease, breathing problem and for improving muscle vitality, formulation and removing toxic substances etc.In addition there is hope in amino acid derivativges in treatment of cancer.
In amino acid preparation process, need to provide suitable reaction environment can realize amino acid whose production efficiency to its reaction high, increase the economic benefit of enterprise, accomplish to optimize the effect of producing.And be that strict management and control is carried out to each processing step in amino acids production process for amino acid whose reaction environment usual method, the personnel cost that its process not only adds enterprise affects production efficiency simultaneously, there is the situation that the inessential waste of material is large.
Summary of the invention
In order to solve the problem, the invention provides and a kind of the environment such as water, gas used required in amino acids production process be carried out centralized management, effectively enhancing productivity and reduce the technical scheme of enterprises using the labor cost simultaneously:
Reaction environment control system in one seed amino acid processing procedure, control system is by air handling system, steam regulating system, form respectively at output conducting after water source parallel join from cooling water source and from the beginning.
Air handling system connects and composes from front to back in a serial fashion by from air-source, control valve A, C level filter, cooling driers, T level filter, A level filter and air cleaner.
Steam regulating system comprises from vapour source, vapor filter and control valve, describedly after vapour source is connected with control valve, is divided into pipeline A and pipeline B, with output conducting after pipeline A is connected with vapor filter, and the direct and output conducting of pipeline B.
Be connected rear and output conducting from cooling water source with control valve B, water source is connected rear and output conducting with control valve C from the beginning.
As preferably, the air total filter that air cleaner is divided into two structures identical and air pre cleaner, air total filter and air pre cleaner one serial mode connect, air pre cleaner and the conducting of A level filter, the direct and output conducting of air total filter.
As preferably, also comprise check-valves, check-valves is connected between A level filter and air pre cleaner in a serial fashion.
As preferably, cooling driers comprises flight flow-guiding type separator, the both sides of flight flow-guiding type separator are respectively arranged with forecooler and cooler, the top of flight flow-guiding type separator is provided with wire gauzee filter, the top of wire gauzee filter is provided with channel partition, the top of forecooler is provided with forecooler end socket, and the upper and lower of cooler is respectively arranged with cooler bulkhead, and the bottom of forecooler is provided with air intake and air outlet slit.
Beneficial effect of the present invention is:
(1) the present invention by air handling system, steam regulating system, from cooling water source and water source centralized Control from the beginning, the condition simultaneously adopting advanced management mode to realize water, gas needed for instant adjustment reflection achieves carries out strict management and control to each processing step, its process is simple, not only decrease the personnel cost of enterprise, effectively improve production efficiency simultaneously, reduce the situation of the inessential loss of material.
(2) the air cleaner air total filter that is divided into two structures identical and air pre cleaner, enhancing airfiltering management and control degree, making operator possess sensitiveer adjustment when monitoring amino acid reflection condition.
(3) in invention, check-valves is connected between A level filter and air pre cleaner in a serial fashion, can effectively avoid the air return after metre filter at different levels thus have influence on output export the parameter of air own, it designs more science, simple and easy.
(4) cooling driers in the present invention is compared with traditional cooling driers, and the heat exchange area of unit volume is higher, and heat exchange efficiency is also higher, by the effectiveness synthesis of air-air preheat interchanger and air-refrigerant heat exchanger in one, simplify piping, package size is greatly reduced, cost reduces.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Fig. 2 is cooling driers structural representation.
Detailed description of the invention
For making goal of the invention of the present invention, technical scheme and advantage clearly, below in conjunction with accompanying drawing, embodiments of the present invention are described in further detail.
As shown in Figure 1, reaction environment control system in a seed amino acid processing procedure, this control system is by air handling system, steam regulating system, form respectively at output 17 conducting after water source 15 parallel join from cooling water source 13 and from the beginning.Air handling system connects and composes from front to back in a serial fashion by from air-source 1, control valve A2, C level filter 3, cooling driers 4, T level filter 5, A level filter 6 and air cleaner 7.Steam regulating system comprises from vapour source 8, vapor filter 9 and control valve 10, pipeline A11 and pipeline B12 is divided into after vapour source 8 is connected with control valve 10, with output 17 conducting after pipeline A11 is connected with vapor filter 9, direct and output 17 conducting of pipeline B12.Be connected rear and output 17 conducting from cooling water source 13 with control valve B14, water source 15 is connected rear and output 17 conducting with control valve C16 from the beginning.By to air handling system, steam regulating system, from cooling water source 13 and water source 15 centralized Control from the beginning, the condition simultaneously adopting advanced management mode to realize water, gas needed for instant adjustment reflection achieves carries out strict management and control to each processing step, its process is simple, not only decrease the personnel cost of enterprise, effectively improve production efficiency simultaneously, reduce the situation of the inessential loss of material.
Simultaneously, the air total filter 7a that air cleaner 7 is divided into two structures identical and air pre cleaner 7b, air total filter 7a and air pre cleaner 7b mono-serial mode connect, air pre cleaner 7b and the conducting of A level filter 6, air total filter 7a directly and output 17 conducting, enhancing airfiltering management and control degree, making operator possess sensitiveer adjustment when monitoring amino acid reflection condition.And set up check-valves 18 at Fang Mingzhong, check-valves 18 is connected between A level filter 6 and air pre cleaner 7b in a serial fashion, can effectively avoid the air return after metre filter at different levels thus have influence on output export the parameter of air own, it designs more science, simple and easy.
As shown in Figure 2, cooling driers 4 comprises flight flow-guiding type separator 4a, the both sides of flight flow-guiding type separator 4a are respectively arranged with forecooler 4b and cooler 4c, the top of flight flow-guiding type separator 4a is provided with wire gauzee filter 4d, the top of wire gauzee filter 4d is provided with channel partition 4e, the top of forecooler 4b is provided with forecooler end socket 4f, and the upper and lower of cooler 4c is respectively arranged with cooler bulkhead 4g, is provided with air intake 4h and air outlet slit 4i in the bottom of forecooler 4b.Compared with traditional cooling driers, the heat exchange area of unit volume is higher, and heat exchange efficiency is also higher, by the effectiveness synthesis of air-air preheat interchanger and air-refrigerant heat exchanger in one, simplifies piping, package size is greatly reduced, and cost reduces.
Above-described embodiment is preferred embodiment of the present invention; it is not the restriction to technical solution of the present invention; as long as without the technical scheme that creative work can realize on the basis of above-described embodiment, all should be considered as falling within the scope of the rights protection of patent of the present invention.
Claims (4)
1. reaction environment control system in a seed amino acid processing procedure, is characterized in that: described control system is by air handling system, steam regulating system, form respectively at output conducting after water source parallel join from cooling water source and from the beginning; Described air handling system connects and composes from front to back in a serial fashion by from air-source, control valve A, C level filter, cooling driers, T level filter, A level filter and air cleaner; Described steam regulating system comprises from vapour source, vapor filter and control valve, describedly after vapour source is connected with control valve, is divided into pipeline A and pipeline B, with output conducting after pipeline A is connected with vapor filter, and the direct and output conducting of pipeline B; Described after cooling water source is connected with control valve B and output conducting; Described water source is from the beginning connected rear and output conducting with control valve C.
2. reaction environment control system in a seed amino acid processing procedure according to claim 1, it is characterized in that: the air total filter that described air cleaner is divided into two structures identical and air pre cleaner, described air total filter and air pre cleaner one serial mode connect, described air pre cleaner and the conducting of A level filter, described air total filter directly and output conducting.
3. reaction environment control system in a seed amino acid processing procedure according to claim 1 and 2, it is characterized in that: also comprise check-valves, described check-valves is connected between A level filter and air pre cleaner in a serial fashion.
4. reaction environment control system in a seed amino acid processing procedure according to claim 1, it is characterized in that: described cooling driers comprises flight flow-guiding type separator, the both sides of flight flow-guiding type separator are respectively arranged with forecooler and cooler, the top of flight flow-guiding type separator is provided with wire gauzee filter, the top of wire gauzee filter is provided with channel partition, the top of forecooler is provided with forecooler end socket, the upper and lower of cooler is respectively arranged with cooler bulkhead, and the bottom of forecooler is provided with air intake and air outlet slit.
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| Application Number | Priority Date | Filing Date | Title |
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| CN201510247805.0A CN105032044A (en) | 2015-08-19 | 2015-08-19 | Reaction environment control system in amino acid production process |
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| CN201510247805.0A CN105032044A (en) | 2015-08-19 | 2015-08-19 | Reaction environment control system in amino acid production process |
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| CN105032044A true CN105032044A (en) | 2015-11-11 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20230171715A (en) * | 2022-06-14 | 2023-12-21 | 씨제이제일제당 (주) | System with reconfigurable multiple pipe for amino acids compatible production and method thereof |
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| CN101664628A (en) * | 2009-09-15 | 2010-03-10 | 王德荣 | Marine pressure varying adsorption nitrogen making system |
| CN101748186A (en) * | 2009-12-29 | 2010-06-23 | 江苏大学 | FSVM-based lysine fermentation process key state variable soft measuring method and system |
| CN202089970U (en) * | 2011-06-20 | 2011-12-28 | 广东蓝宝制药有限公司 | Air inlet system of Compactin fermentation tank |
| CN102839115A (en) * | 2011-10-09 | 2012-12-26 | 南通天华和睿科技创业有限公司 | Fermentation tank air intake device with filter |
| CN204017641U (en) * | 2014-08-21 | 2014-12-17 | 杭州三福机械设备有限公司 | Novel cooling driers |
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2015
- 2015-08-19 CN CN201510247805.0A patent/CN105032044A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101664628A (en) * | 2009-09-15 | 2010-03-10 | 王德荣 | Marine pressure varying adsorption nitrogen making system |
| CN101748186A (en) * | 2009-12-29 | 2010-06-23 | 江苏大学 | FSVM-based lysine fermentation process key state variable soft measuring method and system |
| CN202089970U (en) * | 2011-06-20 | 2011-12-28 | 广东蓝宝制药有限公司 | Air inlet system of Compactin fermentation tank |
| CN102839115A (en) * | 2011-10-09 | 2012-12-26 | 南通天华和睿科技创业有限公司 | Fermentation tank air intake device with filter |
| CN204017641U (en) * | 2014-08-21 | 2014-12-17 | 杭州三福机械设备有限公司 | Novel cooling driers |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR20230171715A (en) * | 2022-06-14 | 2023-12-21 | 씨제이제일제당 (주) | System with reconfigurable multiple pipe for amino acids compatible production and method thereof |
| WO2023243800A1 (en) * | 2022-06-14 | 2023-12-21 | 씨제이제일제당 (주) | Amino acid production system with reconfigurable multiple pipes for compatible production of amino acids and method for configuring same |
| KR102661850B1 (en) | 2022-06-14 | 2024-04-26 | 씨제이제일제당 (주) | System with reconfigurable multiple pipe for amino acids compatible production and method thereof |
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Application publication date: 20151111 |