CN210279146U - Neutralization apparatus is used in tyrosine production - Google Patents
Neutralization apparatus is used in tyrosine production Download PDFInfo
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- CN210279146U CN210279146U CN201920971749.9U CN201920971749U CN210279146U CN 210279146 U CN210279146 U CN 210279146U CN 201920971749 U CN201920971749 U CN 201920971749U CN 210279146 U CN210279146 U CN 210279146U
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Abstract
The utility model discloses a neutralization apparatus is used in tyrosine production, including support, receiving agencies, discharging pipe, retort, heating pipe, neutralization liquid conveyer pipe, glass electrode, PH meter, axis of rotation, stirring vane, solenoid valve, blade diaphragm orifice, hydrolysis liquid conveyer pipe, go up closing cap and agitator motor, install the retort on the support, provide the reaction vessel of neutralization reaction, be connected with the discharging pipe in the bottom of retort, the directional receiving agencies of discharging pipe has the heating pipe in the lower extreme winding of retort, installs the closing cap at the top of retort, it has defeated material hole and mounting hole to open the chisel on the closing cap, installs neutralization liquid conveyer pipe in defeated material hole department, carries neutralization liquid in to the retort through neutralization liquid conveyer pipe. The utility model discloses a stirring and heating provide the favourable environment of neutralization reaction for neutralization speed, the process of neutralization reaction is monitored by the PH meter simultaneously, through solenoid valve and treater, reaches the effect of automatic neutralization.
Description
Technical Field
The utility model relates to an amino acid production facility specifically is a neutralization apparatus is used in tyrosine production.
Background
The amino acid is a compound obtained by replacing hydrogen atoms on carbon atoms of carboxylic acid with amino groups, and the amino acid molecule contains two functional groups of amino groups and carboxyl groups, and the amino acid is a basic substance for forming protein required by animal nutrition, and can play some roles in human body through metabolism, wherein ① synthesizes tissue protein, ② is changed into amino substances such as acid, hormone, antibody, creatine and the like, ③ is changed into carbohydrate and fat, and ④ is oxidized into carbon dioxide, water and urea to generate energy.
Tyrosine is a conditionally essential amino acid and ketogenic amino acid in humans and is therefore commonly used in biochemical research or in the manufacture of nutritional supplements.
In the process of tyrosine production, a neutralization device is needed to be used for neutralizing the raw material hydrolysate, but the existing neutralization device has low neutralization efficiency due to lack of stirring effect.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a neutralization apparatus is used in tyrosine production to solve the problem that proposes in the above-mentioned background art.
In order to achieve the above object, the utility model provides a following technical scheme:
a neutralization device for tyrosine production comprises a support, a material receiving mechanism, a discharging pipe, a reaction tank, a heating pipe, a neutralizing liquid conveying pipe, a glass electrode, a PH meter, a rotating shaft, a stirring blade, an electromagnetic valve, a blade plate hole, a hydrolysate conveying pipe, an upper sealing cover and a stirring motor, wherein the reaction tank is arranged on the support, the reaction container for neutralization reaction is provided, the discharging pipe is connected to the bottom of the reaction tank, the discharging pipe points to the material receiving mechanism, the heating pipe is wound at the lower end of the reaction tank, the upper sealing cover is arranged at the top of the reaction tank, a material conveying hole and a mounting hole are formed in the upper sealing cover, the neutralizing liquid conveying pipe is arranged at the material conveying hole, neutralizing liquid is conveyed into the reaction tank through the neutralizing liquid conveying pipe, the rotating bearing is arranged in the mounting hole, the rotating shaft is arranged in the rotating bearing, and the top of the rotating shaft, the casing of agitator motor is fixed above the upper seal cover, a plurality of stirring vane are installed to the axis of rotation in the inside interval of retort, the last chisel of stirring vane has a plurality of blade diaphragm orifices, through the blade diaphragm orifice when reducing stirring vane's rotating resistance, increase the non-atress region in the stirring vane removal region, destroy the stress balance, reinforcing stirring effect, install the PH meter on the lateral wall of retort, the glass electrode of PH meter is located the retort for detect the PH value of the internal mixing liquid of retort, and the glass electrode is located the outside in stirring vane removal region, prevents that the glass electrode from being broken by pivoted stirring vane, still be connected with the hydrolysate conveyer pipe on the lateral wall of retort for to carry raw materials hydrolysate in the retort, all install the solenoid valve on discharging pipe, neutralization liquid conveyer pipe and the hydrolysate conveyer pipe, the solenoid valve includes solenoid valve an, solenoid valve b and solenoid valve c, and wherein solenoid valve a installs on the discharging pipe, and solenoid valve b installs on the conveying pipe of neutralization liquid, and solenoid valve c installs on the conveying pipe of hydrolysis liquid, and the solenoid valve all connects the output at the treater, and the input at the treater is connected to the PH meter.
As a further aspect of the present invention: the support inner ring is pasted with the shock-absorbing washer to through shock-absorbing washer and retort contact, prevent that agitator motor's operation from leading to retort and support to take place direct collision.
As a further aspect of the present invention: the reaction tank is made of stainless steel materials, and a corrosion-resistant layer is plated on the inner wall of the reaction tank.
As a further aspect of the present invention: the input at the treater is connected to the PH meter through signal line, solenoid valve a, solenoid valve b and solenoid valve c all connect the output at the treater, keep 30 minutes unchangeably when the PH count, and when PH value is less than 4.7, solenoid valve b switch-on, neutralization liquid conveyer pipe is to the interior neutralization liquid of carrying of retort, it is unchangeable when the PH count keeps 30 minutes, and PH value is located 4.7 ~ 5.3, solenoid valve a switch-on, the mixed liquid that stops the neutralization is located the output by the discharging pipe, keep 30 minutes unchangeable when PH count, and when PH value is higher than 5.3, solenoid valve c switch-on, the hydrolysate conveyer pipe is to the interior transport raw materials hydrolysate of retort.
As a further aspect of the present invention: the electromagnetic valve is a polyvinyl chloride chemical engineering electromagnetic valve with the model number of ZCV40 produced by Shanghai Chunfu fluid equipment Limited, and the stirring motor is an asynchronous motor with the model number of 6IK120A-A produced by Changzhou Lun industry electromechanical manufacturing Limited.
Compared with the prior art, the beneficial effects of the utility model are that:
the utility model discloses a stirring and heating provide the favourable environment of neutralization reaction for neutralization speed, the process of neutralization reaction is monitored by the PH meter simultaneously, through solenoid valve and treater, reaches the effect of automatic neutralization.
Drawings
FIG. 1 is a schematic view of a neutralization apparatus for tyrosine production.
FIG. 2 is a block diagram of a neutralization apparatus for tyrosine production.
In the figure: support 1, receiving agencies 2, discharging pipe 3, retort 4, heating pipe 5, neutralization liquid conveyer pipe 6, glass electrode 7, PH meter 8, axis of rotation 9, stirring vane 10, solenoid valve 11, blade diaphragm orifice 12, hydrolysis conveyer pipe 13, upper cover 14 and agitator motor 15.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments. Based on the embodiments in the present invention, all other embodiments obtained by a person skilled in the art without creative work belong to the protection scope of the present invention.
Referring to fig. 1-2, in an embodiment of the present invention, a neutralization apparatus for tyrosine production includes a support 1, a material receiving mechanism 2, a material discharging pipe 3, a reaction tank 4, a heating pipe 5, a neutralization liquid conveying pipe 6, a glass electrode 7, a PH meter 8, a rotating shaft 9, stirring blades 10, a solenoid valve 11, a blade plate hole 12, a hydrolysate conveying pipe 13, an upper sealing cover 14 and a stirring motor 15, wherein the support 1 is provided with the reaction tank 4 for providing a neutralization reaction, the bottom of the reaction tank 4 is connected with the material discharging pipe 3, the material discharging pipe 3 points to the material receiving mechanism 2, the lower end of the reaction tank 4 is wound with the heating pipe 5, the top of the reaction tank 4 is provided with the upper sealing cover 14, the upper sealing cover 14 is provided with material conveying holes and mounting holes, the neutralization liquid conveying pipe 6 is mounted at the material conveying holes, neutralization liquid is conveyed into the reaction tank 4 through the neutralization liquid conveying pipe 6, install rolling bearing in the mounting hole, install axis of rotation 9 in rolling bearing, the top of axis of rotation 9 is connected with agitator motor 15's output shaft, agitator motor 15's casing is fixed in last closing cap 14 top, a plurality of stirring vane 10 are installed to axis of rotation 9 on the inside interval of retort 4, a plurality of blade plate holes 12 have been dug on the stirring vane 10, through blade plate hole 12 when reducing stirring vane 10's rotation resistance, increase the non-atress region in stirring vane 10 removal region, destroy the stress balance, strengthen the stirring effect, install PH meter 8 on retort 4's lateral wall, PH meter 8's glass electrode 7 is located retort 4 for detect the PH value of the internal mixing liquid of retort 4, and glass electrode 7 is located stirring vane 10 removal region's outside, prevent that glass electrode 7 from being smashed by pivoted stirring vane 10, still be connected with hydrolysate conveyer pipe 13 on the lateral wall of retort 4 for carry the raw materials hydrolysate in to retort 4, all install solenoid valve 11 on discharging pipe 3, neutralization liquid conveyer pipe 6 and the hydrolysate conveyer pipe 13, solenoid valve 11 includes solenoid valve an, solenoid valve b and solenoid valve c, and wherein solenoid valve a installs on discharging pipe 3, and solenoid valve b installs on neutralization liquid conveyer pipe 6, and solenoid valve c installs on hydrolysate conveyer pipe 13, and solenoid valve 11 all connects the output at the treater, and the input at the treater is connected to PH meter 8.
A damping washer is pasted on the inner ring of the support 1 and is in contact with the reaction tank 4, so that the direct collision between the reaction tank 4 and the support 1 caused by the operation of the stirring motor 15 is prevented.
The reaction tank 4 is made of stainless steel material, and a corrosion-resistant layer is plated on the inner wall of the reaction tank 4.
PH meter 8 passes through the signal line and connects the input at the treater, solenoid valve a, solenoid valve b and solenoid valve c all connect the output at the treater, keep unchanged for 30 minutes when PH meter 8 registration, and the PH value is less than 4.7, solenoid valve b switch-on, neutralization liquid conveyer pipe 6 is to carrying neutralization liquid in retort 4, keep unchanged for 30 minutes when PH meter 8 registration, and the PH value is located 4.7 ~ 5.3, solenoid valve a switch-on, the mixed liquid that stops the neutralization is located output by discharging pipe 3, keep unchanged for 30 minutes when PH meter 8 registration, and the PH value is higher than 5.3, solenoid valve c switch-on, hydrolysate conveyer pipe 13 is to carrying the raw materials hydrolysate in retort 4.
The electromagnetic valve 11 is a polyvinyl chloride chemical engineering electromagnetic valve with the model number of ZCV40 produced by Shanghai Chunfu fluid equipment Limited, and the stirring motor 15 is an asynchronous motor with the model number of 6IK120A-A produced by Changzhou nationality mechanical and electrical machinery manufacturing Limited.
The utility model discloses a theory of operation is:
tyrosine production raw materials are dissolved by adding acid to obtain raw material hydrolysate, the raw material hydrolysate is conveyed into a reaction tank 4, and then alkaline solution is added to be used as neutralizing solution. By the neutralization reaction in the 8 monitoring retort 4 of PH meter, keep 30 minutes unchangeable when the 8 readings of PH meter, and PH value is less than 4.7, solenoid valve b switch-on, neutralization liquid conveyer pipe 6 is to carrying neutralization liquid in retort 4, keep 30 minutes unchangeable when the 8 readings of PH meter, and PH value is located 4.7 ~ 5.3 time, solenoid valve a switch-on, the mixed liquid of stopping the neutralization is located the output by discharging pipe 3, keep 30 minutes unchangeable when the 8 readings of PH meter, and PH value is higher than 5.3 time, solenoid valve c switch-on, hydrolysate conveyer pipe 13 is to carrying the raw materials hydrolysate in retort 4. The effect of automatic neutralization is achieved, and the mixed solution with the pH value close to 5 is finally obtained, so that the tyrosine can be conveniently prepared in the next step.
Although the present invention has been described in detail with reference to the foregoing embodiments, it will be apparent to those skilled in the art that modifications may be made to the embodiments or portions thereof without departing from the spirit and scope of the invention.
Claims (5)
1. The utility model provides a neutralization apparatus is used in tyrosine production, includes support (1), receiving agencies (2), discharging pipe (3), retort (4), heating pipe (5), neutralization liquid conveyer pipe (6), glass electrode (7), PH meter (8), axis of rotation (9), stirring vane (10), solenoid valve (11), blade diaphragm orifice (12), hydrolysate conveyer pipe (13), go up closing cap (14) and agitator motor (15), its characterized in that: install retort (4) on support (1), be connected with discharging pipe (3) in the bottom of retort (4), directional receiving agencies (2) in discharging pipe (3), lower extreme winding at retort (4) has heating pipe (5), installs closing cap (14) at the top of retort (4), go up closing cap (14) and go up the chisel and have defeated material hole and mounting hole, install neutralization liquid delivery pipe (6) in defeated material hole department, install rolling bearing in the mounting hole, install axis of rotation (9) in rolling bearing, the top of axis of rotation (9) and the output shaft of agitator motor (15), the casing of agitator motor (15) is fixed in last closing cap (14) top, a plurality of stirring vane (10) are installed on the interval of axis of rotation (9) inside retort (4), chisel has a plurality of blade plate holes (12) on stirring vane (10), install PH meter (8) on the lateral wall of retort (4), glass electrode (7) of PH meter (8) are located retort (4), and glass electrode (7) are located stirring vane (10) and remove regional outside, still be connected with hydrolysate conveyer pipe (13) on the lateral wall of retort (4), all install solenoid valve (11) on discharging pipe (3), neutralization liquid conveyer pipe (6) and hydrolysate conveyer pipe (13), solenoid valve (11) include solenoid valve an, solenoid valve b and solenoid valve c, and wherein solenoid valve a installs on discharging pipe (3), and solenoid valve b installs on neutralization liquid conveyer pipe (6), and solenoid valve c installs on hydrolysate conveyer pipe (13), and solenoid valve (11) all connect the output at the treater, and the input at the treater is connected in PH meter (8).
2. A neutralization apparatus for use in the production of tyrosine according to claim 1, wherein: and a damping gasket is pasted on the inner ring of the support (1) and is in contact with the reaction tank (4) through the damping gasket.
3. A neutralization apparatus for use in the production of tyrosine according to claim 1, wherein: the reaction tank (4) is made of stainless steel materials, and a corrosion-resistant layer is plated on the inner wall of the reaction tank (4).
4. A neutralization apparatus for use in the production of tyrosine according to claim 1, wherein: the PH meter (8) is connected to the input end of the processor through a signal line, and the electromagnetic valve a, the electromagnetic valve b and the electromagnetic valve c are connected to the output end of the processor.
5. A neutralization apparatus for use in the production of tyrosine according to claim 1, wherein: the electromagnetic valve (11) is a polyvinyl chloride chemical electromagnetic valve with the model number of ZCV40 produced by Shanghai Chunfu fluid equipment Limited, and the stirring motor (15) is an asynchronous motor with the model number of 6IK120A-A produced by Hezhou nations mechanical and electrical manufacturing Limited.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920971749.9U CN210279146U (en) | 2019-06-26 | 2019-06-26 | Neutralization apparatus is used in tyrosine production |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201920971749.9U CN210279146U (en) | 2019-06-26 | 2019-06-26 | Neutralization apparatus is used in tyrosine production |
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| CN210279146U true CN210279146U (en) | 2020-04-10 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112661313A (en) * | 2020-12-30 | 2021-04-16 | 深圳市正力实业有限公司 | Phosphorite acid waste water cyclic utilization equipment |
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- 2019-06-26 CN CN201920971749.9U patent/CN210279146U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112661313A (en) * | 2020-12-30 | 2021-04-16 | 深圳市正力实业有限公司 | Phosphorite acid waste water cyclic utilization equipment |
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