阅读说明：本技术 果胶生产提取装置及其生产方法 (Pectin production and extraction device and production method thereof ) 是由 魏常昱 于 2021-07-30 设计创作，主要内容包括：本发明提供一种果胶生产提取装置及其生产方法,分离罐外部套设有第一加热套,分离罐内部设有第一网板,第一网板上设有第一网桶,第一网桶开口端通过多根第一提升绳与第一卷扬机连接,分离罐上的盖板还设有第一气缸,第一气缸伸缩端穿过盖板与压板连接,压板设在分离罐内部,所述分离罐通过管道与调节罐连通,调节罐一侧还设有储酸管,储酸管与调节罐连通,还设有净化罐,净化罐与调节罐连通,净化罐一侧还设有乙醇罐,乙醇罐与净化罐连通,还设有烘干房,烘干房与净化罐连接。生产果胶简单,工艺简单,有利于后序工序的提取,大大提高了果胶产率,非常适合工业化连续生产。(The invention provides a pectin production and extraction device and a production method thereof.A first heating sleeve is sleeved outside a separation tank, a first screen plate is arranged inside the separation tank, a first mesh barrel is arranged on the first screen plate, the opening end of the first mesh barrel is connected with a first winch through a plurality of first lifting ropes, a first air cylinder is further arranged on a cover plate on the separation tank, the telescopic end of the first air cylinder penetrates through the cover plate to be connected with a pressing plate, the pressing plate is arranged inside the separation tank, the separation tank is communicated with an adjusting tank through a pipeline, an acid storage pipe is further arranged on one side of the adjusting tank and communicated with the adjusting tank, a purification tank is further arranged, the purification tank is communicated with the adjusting tank, an ethanol tank is further arranged on one side of the purification tank and communicated with the purification tank, and a drying room is further arranged, and the drying room is connected with the purification tank. The pectin is simple to produce, the process is simple, the extraction of subsequent procedures is facilitated, the pectin yield is greatly improved, and the method is very suitable for industrial continuous production.)

1. The utility model provides a pectin production extraction element, characterized by: comprises a separation tank (3), a first heating sleeve (2) is sleeved outside the separation tank (3), a first screen plate (4) is arranged inside the separation tank (3), a first screen barrel (5) is arranged on the first screen plate (4), the open end of the first screen barrel (5) is connected with a first winch (11) through a plurality of first lifting ropes (6), a first air cylinder (9) is further arranged on a cover plate (7) on the separation tank (3), the telescopic end of the first air cylinder (9) penetrates through the cover plate (7) to be connected with a pressing plate (8), the pressing plate (8) is arranged inside the separation tank (3), the separation tank (3) is communicated with an adjusting tank (13) through a pipeline, an acid storage pipe (16) is further arranged on one side of the adjusting tank (13), the acid storage pipe (16) is communicated with the adjusting tank (13), a purification tank (17) is further arranged, the purification tank (17) is communicated with the adjusting tank (13), an ethanol tank (22) is further arranged on one side of the purification tank (17), the ethanol tank (22) is communicated with the purification tank (17), and is also provided with a drying room (24), and the drying room (24) is connected with the purification tank (17).

2. The pectin production and extraction device of claim 1, wherein: first net bucket (5) open end is equipped with lifting platform (501), and lifting platform (501) extend to knockout drum (3) outside, and many first lifting ropes (6) are connected with lifting platform (501).

3. The pectin production and extraction device of claim 2, wherein: still be equipped with a plurality of second cylinders (10) on apron (7), second cylinder (10) one end is connected with apron (7), and the other end is connected with the wall body, still is equipped with blast pipe (12) on apron (7).

4. The pectin production and extraction device of claim 2, wherein: the water storage tank (1) is further arranged, the water storage tank (1) is communicated with a water inlet (303) of the separation tank (3) through a pump body, and a water outlet (302) of the separation tank (3) is communicated with a water outlet.

5. The pectin production and extraction device of claim 1, wherein: a liquid discharge port (301) of the water storage tank (1) is communicated with a raw material filling port (1301) of an adjusting tank (13) through a pump body, a second screen plate (15) is arranged inside the adjusting tank (13), and the raw material filling port (1301) is arranged above the second screen plate (15).

6. The pectin production and extraction device of claim 1, wherein: the acid storage pipe (16) is communicated with the adjusting tank (13) through a dosing pump, and a second heating sleeve (14) is sleeved outside the adjusting tank (13).

7. The pectin production and extraction device of claim 1, wherein: a third net barrel (18) is arranged in the purification tank (17), and the outer surface of the third net barrel (18) is close to the inner surface of the purification tank (17).

8. The pectin production and extraction device of claim 7, wherein: and a plurality of second winches (19) are also arranged, and the second winches (19) are connected with the third net barrel (18) through second lifting ropes (20).

9. The pectin production and extraction device of claim 7, wherein: the ethanol tank (22) is communicated with the purification tank (17) through a dosing pump, the purification tank (17) is communicated with the ethanol purification device (23) through a pump body, and the ethanol purification device (23) is communicated with the ethanol tank (22);

a lifting machine (21) is also arranged above the purification tank (17), and the lifting machine (21) is communicated with the drying room (24) through a conveying belt;

the third net barrel (18) is lifted, and the lower end of the lifter (21) is close to the bottom of the third net barrel (18).

10. The method for producing pectin producing and extracting device according to any one of claims 1-9, characterized by: the method comprises the following steps:

s1, adding water into the separating tank (3) through the water storage tank (1), placing the manufactured raw materials in the first net barrel (5), placing the first net barrel (5) into the separating tank (3) through the first winch (11), and sealing the cover plate (7) on the separating tank (3) through the second cylinder (10);

s2, heating the separation tank (3) by the first heating sleeve (2), and steaming the raw materials in the separation tank (3) for 30-40 minutes to kill pectinase in living cells;

s3, controlling a pressing plate (8) to move downwards by a first air cylinder (9), squeezing the raw materials for multiple times, lifting raw material slag by a first mesh barrel (5) after squeezing, discharging, and conveying water steamed in a separation tank (3) and squeezed stock solution into a regulating tank (13);

s4, filtering the stock solution through a second screen plate (15), adding acid liquor into an adjusting tank (13) through an acid storage pipe (16), adjusting the pH value to 2-3, adding 0.3-0.5% of activated carbon into the adjusting tank (13) for decoloring, heating a second heating sleeve (14) to 60-70 ℃, and heating for 30-50 minutes;

s5, conveying the adjusted stock solution into a purification tank (17), cooling to normal temperature, adding an ethanol solution into the purification tank (17), reacting for 30-50 minutes, beginning to flocculate, lifting the whole third mesh barrel (18) by using a second lifting rope (20) after flocculation, and separating flocculated substances from the solution;

s6, lifting the third mesh bucket (18) by the second lifting rope (20), wherein the bottom of the third mesh bucket (18) is close to the bottom of the lifter (21), and the lifter (21) lifts the flocculated substances in the third mesh bucket (18) to a conveyor;

s7, conveying the flocculated substances to a drying room (24), drying the flocculated substances at 75-85 ℃, grinding after drying, and storing the ground pectin powder.

Technical Field

The invention relates to the field of pectin production, in particular to a pectin production and extraction device and a production method thereof.

Background

Pectin is a galacturonic acid high-molecular polymer constituting a cell structural component, and is widely present in cell walls of roots, stems, leaves and fruits of various plants. Practice proves that the pectin has the effects of resisting cancers, removing heavy metals in vivo, regulating blood sugar and reducing blood fat, can effectively combine lead in intestinal tracts of a human body to prevent the lead from being absorbed by the human body and be discharged out of the human body along with feces, but the natural pectin has larger molecular chains and cannot be absorbed by the human body, so that the lead and bone lead in blood of the human body cannot be effectively removed, the reasonable molecular weight is important for achieving the functions of resisting cancers, removing heavy metals in blood and the like of the high-activity pectin, the molecular weight is too large to be absorbed by the human body, and if the molecular weight is too small, the pectin cannot play a role in chelating galectin, heavy metals and the like.

The raw materials for industrial production of pectin mainly comprise apple pomace and citrus fruit peel, in the production process, partial pomace has poor worry effect, the efficiency of producing pectin by the traditional process is poor, the automation degree of production equipment is low, improper treatment can cause the purity of a pectin finished product to be reduced, the color of the pectin finished product to be darkened, and the quality of the product to be degraded.

Disclosure of Invention

The invention mainly aims to provide a pectin production and extraction device and a production method thereof, and solves the problems of poor efficiency and low automation degree of production equipment in the traditional process for producing pectin.

In order to solve the technical problems, the technical scheme adopted by the invention is as follows: the utility model provides a pectin production extraction element, includes the knockout drum, and the outside cover of knockout drum is equipped with first heating jacket, and the inside first otter board that is equipped with of knockout drum is equipped with first net bucket on the first otter board, and first net bucket open end is connected with first hoisting machine through many first lifting ropes, and the apron on the knockout drum still is equipped with first cylinder, and the flexible end of first cylinder passes the apron to be connected with the clamp plate, and the clamp plate is established inside the knockout drum, the knockout drum passes through pipeline and adjusting pot intercommunication, and adjusting pot one side still is equipped with stores up the acid pipe, stores up acid pipe and adjusting pot intercommunication, still is equipped with the purifying tank, and purifying tank and adjusting pot intercommunication still are equipped with the ethanol jar on one side, and ethanol jar and purifying tank intercommunication still are equipped with the stoving room, and the stoving room is connected with the purifying tank.

In the preferred scheme, first net bucket open end is equipped with the lifting platform, and the lifting platform extends to the knockout drum outside, and many first lifting ropes are connected with the lifting platform.

In the preferred scheme, still be equipped with a plurality of second cylinders on the apron, second cylinder one end and apron are connected, and the other end and wall connection still are equipped with the blast pipe on the apron.

In the preferred scheme, a water storage tank is further arranged, the water storage tank is communicated with a water inlet of the separation tank through a pump body, and a water outlet of the separation tank is communicated with a water outlet.

In the preferred scheme, the leakage fluid dram of storage water tank passes through the raw materials filling opening intercommunication of the pump body with the surge drum, and surge drum inside is equipped with the second otter board, and the raw materials filling opening is established in second otter board top.

In the preferred scheme, the acid storage pipe is communicated with the adjusting tank through a dosing pump, and a second heating sleeve is sleeved outside the adjusting tank.

In the preferred scheme, the inside third wire barrel that is equipped with of purifying tank, third wire barrel surface are close to the purifying tank inner surface.

In the preferred scheme, a plurality of second winches are further arranged and are connected with the third net barrel through second lifting ropes.

In the preferred scheme, the ethanol tank is communicated with the purification tank through a dosing pump, the purification tank is communicated with the ethanol purification device through a pump body, and the ethanol purification device is communicated with the ethanol tank.

In the preferred scheme, a lifting machine is also arranged above the purification tank and is communicated with the drying room through a conveying belt;

the third net barrel rises, and the lower end of the elevator is close to the bottom of the third net barrel.

The method comprises the following steps:

s1, adding water into the separation tank through the water storage tank, placing the manufactured raw materials in the first net barrel, placing the first net barrel into the separation tank through the first winch, and sealing the cover plate on the separation tank through the second cylinder;

s2, heating the separation tank by the first heating sleeve, and steaming the raw materials in the separation tank for 30-40 minutes to kill pectinase in living cells;

s3, controlling a pressing plate to face downwards by a first cylinder, squeezing the raw materials for multiple times, lifting raw material slag by a first mesh barrel after squeezing, discharging, and conveying the water evaporated in the separation tank and the squeezed stock solution to the interior of a regulating tank;

s4, filtering the stock solution through a second screen plate, adding an acid solution in an adjusting tank through an acid storage tube, adjusting the pH value to 2-3, adding 0.3-0.5% of activated carbon into the adjusting tank for decolorization, heating the mixture to 60-70 ℃ by a second heating sleeve, and heating for 30-50 minutes;

s5, conveying the adjusted stock solution into a purification tank, cooling to normal temperature, adding an ethanol solution into the purification tank, reacting for 30-50 minutes, beginning to flocculate, lifting the whole third mesh barrel by using a second lifting rope after flocculation, and separating flocculated substances from the solution;

s6, lifting a third mesh bucket by the second lifting rope, wherein the bottom of the third mesh bucket is close to the bottom of the lifting machine, and the lifting machine lifts flocculated substances in the third mesh bucket onto the conveyor;

s7, conveying the flocculated substances to a drying room, drying the flocculated substances at 75-85 ℃, grinding after drying, and storing the ground pectin powder.

The invention provides a pectin production and extraction device and a production method thereof, wherein a separation tank is used for boiling and softening raw materials, water in the separation tank is discharged after softening, a pressing plate is used for squeezing the raw materials, the squeezed solution enters a regulating tank for secondary filtration, part of raw material residues are filtered, the solution is added with water to regulate the pH value, then the solution is heated in the regulating tank, the solution after the acid regulation treatment enters a purifying tank, the pectin solution in the purifying tank is flocculated by ethanol in the ethanol tank, the flocculated and filtered substances are lifted to the inside of a drying room by a lifter for drying to form pectin, and the pectin is stored.

Drawings

The invention is further illustrated by the following examples in conjunction with the accompanying drawings:

FIG. 1 is a diagram of the overall connection architecture of the present invention;

FIG. 2 is a diagram of a separator tank of the present invention;

FIG. 3 is a view of a third net barrel according to the present invention;

in the figure: a water storage tank 1; a first heating mantle 2; a separation tank 3; a liquid discharge port 301; a water outlet 302; a water inlet 303; a first net plate 4; a first net barrel 5; a lift stage 501; a first lift cord 6; a cover plate 7; a pressing plate 8; a first cylinder 9; a second cylinder 10; a first hoist 11; an exhaust pipe 12; a conditioning tank 13; a raw material charging port 1301; a second heating mantle 14; a second net plate 15; an acid storage tube 16; a purge tank 17; a third net barrel 18; a second hoist 19; a second lift cord 20; a hoist 21; an ethanol tank 22; an ethanol purification device 23; a drying room 24.

Detailed Description

Example 1

As shown in figures 1-3, a pectin production and extraction device comprises a separation tank 3, a first heating jacket 2 is sleeved outside the separation tank 3, a first screen plate 4 is arranged inside the separation tank 3, a first screen barrel 5 is arranged on the first screen plate 4, the open end of the first screen barrel 5 is connected with a first winch 11 through a plurality of first lifting ropes 6, a first cylinder 9 is further arranged on a cover plate 7 on the separation tank 3, the telescopic end of the first cylinder 9 penetrates through the cover plate 7 to be connected with a pressing plate 8, the pressing plate 8 is arranged inside the separation tank 3, the knockout drum 3 passes through the pipeline and communicates with the surge tank 13, and surge tank 13 one side still is equipped with stores up sour pipe 16, stores up sour pipe 16 and surge tank 13 intercommunication, still is equipped with purifying tank 17, and purifying tank 17 and surge tank 13 intercommunication still are equipped with ethanol jar 22 on one side of purifying tank 17, and ethanol jar 22 and purifying tank 17 intercommunication still are equipped with stoving room 24, and stoving room 24 is connected with purifying tank 17. The separation tank 3 is used for boiling and softening the raw material, water in the separation tank 3 is discharged after softening, the raw material is squeezed by a pressure plate 8, the squeezed solution enters the regulating tank 13 for secondary filtration, part of the raw material slag is filtered, the solution is added with water to regulate the PH value, then the solution is heated in the adjusting tank 13, the solution after the acid adjusting treatment enters the purifying tank 17, the pectin solution in the purification tank 17 is flocculated by the ethanol in the ethanol tank 22, the flocculated and filtered substances are lifted to the inside of the drying room 24 by the lifter 21 to be dried to form pectin, the pectin is stored, the pectin production is simple, the process is simple, the extraction of subsequent procedures is facilitated, the pectin yield is greatly improved, the method is very suitable for industrial continuous production, and after the ethanol is mixed with the liquid pectin solution, water and impurity substances in the pectin solution are absorbed, so that the pectin quality is purified.

In the preferred scheme, first net bucket 5 open end is equipped with elevating platform 501, and elevating platform 501 extends to the knockout drum 3 outside, and many first lifting ropes 6 are connected with elevating platform 501. The structure of the lifting platform 501 is as shown in fig. 2, so that the cover plate 7 and the separation tank 3 are conveniently compressed and sealed, and the first mesh barrel 5 is used for filtering a large amount of raw material slag.

In the preferred scheme, still be equipped with a plurality of second cylinders 10 on the apron 7, second cylinder 10 one end is connected with apron 7, and the other end is connected with the wall body, still is equipped with blast pipe 12 on the apron 7. The second cylinder 10 facilitates lifting the cover plate 7.

In the preferred scheme, a water storage tank 1 is further arranged, the water storage tank 1 is communicated with a water inlet 303 of the separation tank 3 through a pump body, and a water outlet 302 of the separation tank 3 is communicated with a water outlet. As shown in the structure of fig. 1-2, the separating tank 3 is communicated with the water storage tank 1, and the boiled water and the filtered water in the separating tank 3 are added into the adjusting tank 13 together for acid adjusting treatment.

In the preferred scheme, a liquid outlet 301 of the water storage tank 1 is communicated with a raw material filling opening 1301 of the adjusting tank 13 through a pump body, a second screen plate 15 is arranged inside the adjusting tank 13, and the raw material filling opening 1301 is arranged above the second screen plate 15. The inside a large amount of impurity and dregs that contain of storage water tank 1, raw materials filling opening 1301 installs in second otter board 15 top, utilizes second otter board 15 to filter a large amount of impurity and dregs.

In the preferred scheme, the acid storage pipe 16 is communicated with the adjusting tank 13 through a dosing pump, and a second heating sleeve 14 is sleeved outside the adjusting tank 13. The second heating jacket 14 acts as a heating element to accelerate the reaction.

In a preferred scheme, a third mesh barrel 18 is arranged inside the purification tank 17, and the outer surface of the third mesh barrel 18 is close to the inner surface of the purification tank 17. The third mesh bucket 18 serves to filter the flocculated material.

In a preferred scheme, a plurality of second winches 19 are further arranged, and the second winches 19 are connected with the third net barrel 18 through second lifting ropes 20. The second winch 19 lifts the third net drum 18.

In the preferred scheme, the ethanol tank 22 is communicated with the purification tank 17 through a dosing pump, the purification tank 17 is communicated with the ethanol purification device 23 through a pump body, and the ethanol purification device 23 is communicated with the ethanol tank 22. The ethanol in the ethanol tank 22 acts to flocculate the pectin. The ethanol purifies and purifies the ethanol in the purifying tank 17.

In the preferred scheme, still be equipped with lifting machine 21 above purification tank 17, lifting machine 21 passes through the conveyer belt and communicates with stoving room 24, and third net bucket 18 rises, and lifting machine 21 low end is close to third net bucket 18 bottom. With the structure shown in fig. 3, most of the flocculated matters enter the inside of the third mesh bucket 18, and the flocculated matters in the inside of the third mesh bucket 18 are conveyed to the inside of the drying room 24 for drying by the lifter 21.

Example 2

To explain further with reference to embodiment 1, as shown in fig. 1 to 3, a water storage tank 1 adds water into a separation tank 3, the manufactured raw material is placed in a first net barrel 5, a first winch 11 places the first net barrel 5 in the separation tank 3, and a cover plate 7 is sealed on the separation tank 3 by a second cylinder 10.

The first heating jacket 2 heats the separation tank 3, and the raw material is steamed for 30-40 minutes inside the separation tank 3 to kill the pectinase in the living cells.

The first cylinder 9 controls the pressing plate 8 to press the raw material for multiple times, after pressing, the raw material slag is lifted by the first mesh barrel 5 and then discharged, and the water evaporated in the separation tank 3 and the pressed stock solution are conveyed into the adjusting tank 13.

Filtering the stock solution by a second screen 15, adding acid solution into an adjusting tank 13 through an acid storage tube 16, adjusting the pH value to 2-3, adding 0.3-0.5% of activated carbon into the adjusting tank 13 for decolorization, heating a second heating sleeve 14 to 60-70 ℃, and heating for 30-50 minutes.

And (3) conveying the adjusted stock solution into the purification tank 17, cooling to normal temperature, adding an ethanol solution into the purification tank 17, reacting for 30-50 minutes, beginning to flocculate, lifting the whole third net barrel 18 by using the second lifting rope 20 after flocculation, and separating flocculated substances from the solution.

The second lifting rope 20 lifts the third mesh bucket 18, the bottom of the third mesh bucket 18 is close to the bottom of the lifter 21, and the lifter 21 lifts the flocculated substances in the third mesh bucket 18 to the conveyor.

Conveying the flocculated substances to a drying room 24, drying the flocculated substances at 75-85 ℃, grinding after drying, and storing the ground pectin powder.

The above-described embodiments are merely preferred embodiments of the present invention, and should not be construed as limiting the present invention, and the scope of the present invention is defined by the claims, and equivalents including technical features described in the claims. I.e., equivalent alterations and modifications within the scope hereof, are also intended to be within the scope of the invention.