CN112934491A - Separation device for producing oil from walnut endophytic bacterium HB1310 fermentation cotton stalk hydrolysis sugar liquid - Google Patents
Separation device for producing oil from walnut endophytic bacterium HB1310 fermentation cotton stalk hydrolysis sugar liquid Download PDFInfo
- Publication number
- CN112934491A CN112934491A CN202110123096.0A CN202110123096A CN112934491A CN 112934491 A CN112934491 A CN 112934491A CN 202110123096 A CN202110123096 A CN 202110123096A CN 112934491 A CN112934491 A CN 112934491A
- Authority
- CN
- China
- Prior art keywords
- heat exchange
- box
- pipe
- heating
- hot water
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04B—CENTRIFUGES
- B04B15/00—Other accessories for centrifuges
- B04B15/02—Other accessories for centrifuges for cooling, heating, or heat insulating
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The invention discloses an oil production separation device for a hydrolyzed liquid sugar solution of walnut endophytic bacteria HB1310 fermented cotton stalks, which comprises a heating mechanism, a heat exchange mechanism, a material conveying mechanism, a separation mechanism, a preheating mechanism and an installation mechanism; the heating mechanism is fixedly arranged right above the heat exchange mechanism, the heat exchange mechanism is communicated with the heating mechanism through fluid, the heat exchange mechanism is fixedly arranged on the upper surface of the mounting mechanism, the material conveying mechanism is arranged on the left side of the heat exchange mechanism and penetrates through the heat exchange mechanism, the separation mechanism is arranged on the right side of the heat exchange mechanism, the separation mechanism is communicated with the material conveying mechanism through fluid, and the separation mechanism is communicated with the heating mechanism through fluid of the preheating mechanism; according to the invention, the heating mechanism is arranged, so that the centrifuge can be preheated before the centrifuge works, and the fermentation liquor can be continuously heated during the work, so that the separation difficulty caused by the emulsification of the grease in the fermentation liquor can be prevented.
Description
Technical Field
The invention relates to the technical field of microbial oil separation. In particular to a device for separating oil produced by hydrolyzing a sugar solution by fermenting cotton stalks with walnut endophytic bacteria HB 1310.
Background
The invention provides a device for solving the problem that microbial oil produced by hydrolyzing sugar liquor by fermenting cotton stalks with endophytic bacteria HB1310 of walnuts is biosynthesized and converted by using microorganisms such as yeast, mould, bacteria, algae and the like under a certain condition and using carbohydrates, hydrocarbons and common oil as nitrogen sources, carbon sources, trace elements and the like.
Disclosure of Invention
Therefore, the technical problem to be solved by the invention is to provide the device for producing the oil by fermenting the cotton stalk hydrolyzed sugar liquid by the walnut endophytic bacteria HB1310 by using a heating method to prevent oil emulsification.
In order to solve the technical problems, the invention provides the following technical scheme: the separation device for producing oil from the hydrolyzed liquid glucose of the walnut endophytic bacteria HB1310 fermented cotton stalks comprises a heating mechanism, a heat exchange mechanism, a material conveying mechanism, a separation mechanism, a preheating mechanism and an installation mechanism;
heating mechanism fixed mounting is directly over heat exchange mechanism, just heat exchange mechanism and heating mechanism fluid intercommunication, heat exchange mechanism fixed mounting is at the upper surface of installation mechanism, defeated material mechanism sets up in heat exchange mechanism's left side, and defeated material mechanism runs through the inside setting of heat exchange mechanism, separating mechanism sets up on heat exchange mechanism right side, separating mechanism and defeated material mechanism fluid intercommunication, just separating mechanism and heating mechanism are through preheating mechanism fluid intercommunication.
The device for separating the oil from the hydrolyzed sugar liquor of the walnut endophytic bacteria HB1310 fermented cotton stalks comprises a heating mechanism, a first valve, a second valve, an electric box, a connecting rod and a heating wire, wherein the heating mechanism comprises a heating box, a supporting rod, a water inlet pipe, the first valve, a water outlet pipe and the second valve;
the heating box is a square box body and is made of insulating materials, the heating box is fixedly arranged right above the heat exchange mechanism through supporting rods, the number of the supporting rods is four, and the four supporting rods are respectively and fixedly arranged at the four corners of the bottom of the heating box;
a water inlet pipe is fixedly installed on one side of the heating box, the water inlet pipe is located at a position, close to the top, of one side of the heating box, and a first valve is arranged on the water inlet pipe; a water outlet pipe is fixedly arranged on the other side of the heating box, is positioned at a position close to the bottom end of one side of the heating box, and is provided with a second valve;
an electric box is fixedly arranged at the top of the heating box and is positioned in the center of the top of the heating box; the bottom of the heating box is fixedly provided with two connecting rods, the two connecting rods penetrate through the top wall of the heating box and extend into the heating box, and the two connecting rods are symmetrically arranged; two the cavity has all been seted up to the inside of connecting rod, two the inside heater strip that all is provided with of cavity, two heater strip top in the cavity all is connected with the electronic box, just the heater strip of two cavity bottoms interconnects and exposes in the heating cabinet.
The device for separating the oil produced by the hydrolyzed sugar liquor of the walnut endophytic bacteria HB1310 fermented cotton stalks comprises a heat exchange box, a first hot water pipe, a first water pump, an upper heat exchange fin, a phase change material and a lower heat exchange fin;
the heat exchange box is fixedly arranged on the upper surface of the mounting mechanism, the heat exchange box is in a square box body shape, and the area of the upper surface of the heat exchange box is equal to that of the lower surface of the heating box;
the lower surface of the heating box is fixedly provided with a first hot water pipe, a water inlet of the first hot water pipe is positioned at a position, close to the right end, of the lower surface of the heating box, a water outlet of the first hot water pipe is positioned at a position, close to the left end, of the lower surface of the heating box, a top wall of the heat exchange box penetrates through the first hot water pipe and passes through the interior of the heat exchange box, the part, located inside the heat exchange box, of the first hot water pipe is arranged in a multi-layer bending mode, the upper surface of the heat exchange box is fixedly provided with a first water pump, and the first water pump is connected with one end;
an upper heat exchange fin is fixedly arranged in the heat exchange box, the upper surface of the upper heat exchange fin is tightly connected with the first hot water pipe, a phase change material is fixedly arranged in the heat exchange box, and the top of the phase change material is matched with the fins on the lower surface of the upper heat exchange fin; the heat exchange box is characterized in that lower heat exchange fins are fixedly mounted inside the heat exchange box, fins on the upper surfaces of the lower heat exchange fins are matched with the bottom end of the phase change material, and a certain position is reserved in the heat exchange box at the bottom of each lower heat exchange fin.
The device for separating the hydrolyzed sugar liquor and the produced oil of the cotton stalks fermented by the walnut endophytic bacteria HB1310 comprises a material storage tank, a liquid conveying pipe, a second water pump and a temperature measuring instrument;
the material storage box is fixedly arranged on the upper surface of the mounting mechanism, the material storage box is positioned on the left side of the heat exchange box, a liquid conveying pipe is fixedly arranged at the bottom of one side of the material storage box, the liquid conveying pipe penetrates through the two sides of the heat exchange box and is communicated with fluid of the separating mechanism, the liquid conveying pipe is positioned in the heat exchange box and is arranged in a multi-layer bending mode, and the upper surfaces of the parts, positioned in the heat exchange box, of the liquid conveying pipe are tightly connected with the lower surfaces of the lower heat;
the second water pump is fixedly arranged on the upper surface of the mounting mechanism, is connected with the liquid conveying pipe and is positioned between the liquid storage tank and the heat exchange tank; the temperature measuring instrument is fixedly installed on the upper surface of the installation mechanism, and the temperature measuring instrument is connected with the position of the infusion tube, which is out of the heat exchange box.
The separation mechanism comprises a centrifuge, a cavity and a water outlet;
the centrifugal machine is fixedly mounted on the upper surface of the mounting mechanism, the cavity is located inside the centrifugal machine, the water outlet penetrates through the centrifugal machine to be connected with the cavity, and the water outlet is located at the bottom of the cavity.
The device for separating the oil from the hydrolyzed sugar liquor produced by fermenting the cotton stalks by the walnut endophytic bacteria HB1310 comprises a preheating mechanism, a first hot water pipe, a first valve, a first water pump, a return pipe, a second valve and a second water pump;
the water inlet end of the second hot water pipe is connected with the bottom end of one side of the heating box, and the water inlet end of the second hot water pipe and the first hot water pipe are positioned on the same side; the second hot water pipe is provided with a third valve, and the third valve is positioned at the water inlet end of the first hot water pipe; the water outlet end of the second hot water pipe is connected with the cavity, a third water pump is fixedly mounted on the upper surface of the centrifugal machine, and the third water pump is connected with the second hot water pipe;
the water inlet end of the return pipe is connected with the water outlet, the water outlet end of the return pipe is connected with the water inlet formed in the upper surface of the heating box, a fourth valve is fixedly mounted on one side of the centrifugal machine and connected with the return pipe, and a fourth water pump is fixedly mounted on the upper surface of the mounting mechanism and connected with the return pipe.
The walnut endophytic bacterium HB1310 fermented cotton stalk hydrolyzed sugar liquid produced oil separation device comprises an installation mechanism and an anti-slip mat, wherein the installation mechanism comprises a base and a base;
the non-slip mat is made of non-slip materials and fixedly mounted on the lower surface of the base.
The technical scheme of the invention achieves the following beneficial technical effects:
1. according to the invention, the heating mechanism is arranged, so that the centrifugal machine can be preheated before the centrifugal machine works, and the fermentation liquor can be continuously heated during the working, so that the separation difficulty caused by the emulsification of the grease in the fermentation liquor can be prevented; before working, enough clear water is added into a heating box to electrify a heating wire, the clear water in the heating box is heated to a certain degree, a third valve and a fourth valve are opened, a third water pump is opened to lead hot water in the heating box to a cavity of a centrifuge to preheat the cavity, a fourth water pump is opened to lead the clear water in the cavity to be pumped into the heating box through a return pipe, thereby the clear water can be recycled, after the cavity is preheated, a first water pump is opened to lead the hot water in the heating box to circulate through a first hot water pipe, when the hot water passes through a heat exchange box, an upper heat exchange fin can absorb the heat in the first hot water pipe, then the heat is stored in a phase change material, a second water pump is opened to lead fermentation liquor in a liquid storage box to enter the cavity of the centrifuge through a liquid transfer pipe, when the fermentation liquor in the liquid transfer pipe passes through the heat exchange box, the heat in the phase-change material is conducted to the fermentation liquor through the lower heat exchange fins, so that the purpose of heating the fermentation liquor is achieved.
2. According to the invention, the phase-change material is arranged, so that heat in hot water can be rapidly exchanged with the fermentation liquor, and the purpose of continuously heating the fermentation liquor is achieved.
3. According to the invention, the temperature of the fermentation liquor subjected to heat exchange can be observed by arranging the temperature measuring instrument, so that the temperature of the heating box can be adjusted by a worker in time.
4. According to the invention, by arranging the return pipe, the clean water can be repeatedly utilized, and resource waste is avoided.
Drawings
FIG. 1 is a schematic cross-sectional view of the present invention;
FIG. 2 is a schematic side view of the heat exchange box of the present invention;
the reference numbers in the figures denote: 100-a heating mechanism; 200-a heat exchange mechanism; 300-a material conveying mechanism; 400-a separation mechanism; 500-preheating mechanism; 600-a mounting mechanism; 101-a heating box; 102-a support bar; 103-a water inlet pipe; 104-a first valve; 105-a water outlet pipe; 106-a second valve; 107-electric box; 108-a connecting rod; 109-heating wires; 201-heat exchange box; 202-a first hot water pipe; 203-a first water pump; 204-upper heat exchange fins; 205-a phase change material; 206-lower heat exchange fins; 301-a storage bin; 302-an infusion tube; 303-a second water pump; 304-a temperature measuring instrument; 401-centrifuge; 402-a cavity; 403-water outlet; 501-a second hot water pipe; 502-a third valve; 503-a third water pump; 504-a return conduit; 505-a fourth valve; 506-a fourth water pump; 601-a base; 602-non-slip mat.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all of the embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments given herein without making any creative effort, shall fall within the protection scope of the present invention.
The separation device for producing oil from the hydrolyzed sugar liquor of the walnut endophytic bacteria HB1310 fermented cotton stalks comprises a heating mechanism 100, a heat exchange mechanism 200, a material conveying mechanism 300, a separation mechanism 400, a preheating mechanism 500 and an installation mechanism 600; heating mechanism 100 is fixed mounting directly over heat exchange mechanism 200, and heat exchange mechanism 200 and heating mechanism 100 fluid intercommunication, heat exchange mechanism 200 fixed mounting is on the upper surface of installation mechanism 600, defeated material mechanism 300 sets up the left side at heat exchange mechanism 200, and defeated material mechanism 300 runs through the inside setting of heat exchange mechanism 200, separating mechanism 400 sets up on heat exchange mechanism 200 right side, separating mechanism 400 and defeated material mechanism 300 fluid intercommunication, and separating mechanism 400 and heating mechanism 100 are through preheating mechanism 500 fluid intercommunication.
As shown in fig. 1-2, the heating mechanism 100 includes a heating box 101, a support rod 102, a water inlet pipe 103, a first valve 104, a water outlet pipe 105, a second valve 106, an electric box 107, a connecting rod 108, and a heating wire 109; the heating box 101 is a square box body, the heating box 101 is made of an insulating material, the heating box 101 is fixedly arranged right above the heat exchange mechanism 200 through support rods 102, the number of the support rods 102 is four, and the four support rods 102 are respectively and fixedly arranged at the four corners of the bottom of the heating box 101; a water inlet pipe 103 is fixedly installed on one side of the heating box 101, the water inlet pipe 103 is located at a position close to the top of one side of the heating box 101, and a first valve 104 is arranged on the water inlet pipe 103; a water outlet pipe 105 is fixedly installed on the other side of the heating box 101, the water outlet pipe 105 is positioned at a position close to the bottom end of one side of the heating box 101, and a second valve 106 is arranged on the water outlet pipe 105; an electric box 107 is fixedly installed at the top of the heating box 101, and the electric box 107 is positioned at the center of the top of the heating box 101; the bottom of the heating box 101 is fixedly provided with two connecting rods 108, the two connecting rods 108 extend into the heating box 101 through the top wall of the heating box 101, and the two connecting rods 108 are symmetrically arranged; cavities are formed in the two connecting rods 108, heating wires 109 are arranged in the two cavities, the top ends of the heating wires 109 in the two cavities are connected with the electric box 107, and the heating wires 109 at the bottom ends of the two cavities are connected with each other and exposed in the heating box 101; the heat exchange mechanism 200 comprises a heat exchange box 201, a first hot water pipe 202, a first water pump 203, upper heat exchange fins 204, a phase change material 205 and lower heat exchange fins 206; the heat exchange box 201 is fixedly arranged on the upper surface of the mounting mechanism 600, the heat exchange box 201 is a square box body, and the area of the upper surface of the heat exchange box 201 is equal to that of the lower surface of the heating box 101; a first hot water pipe 202 is fixedly installed on the lower surface of the heating box 101, a water inlet of the first hot water pipe 202 is located at a position, close to the right end, of the lower surface of the heating box 101, a water outlet of the first hot water pipe 202 is located at a position, close to the left end, of the lower surface of the heating box 101, the first hot water pipe 202 penetrates through the top wall of the heat exchange box 201 and passes through the interior of the heat exchange box 201, the portion, located inside the heat exchange box 201, of the first hot water pipe 202 is in multi-layer bending arrangement, a first water pump 203 is fixedly installed on the upper surface of the heat exchange box 201, and the first water pump 203 is connected; an upper heat exchange fin 204 is fixedly installed inside the heat exchange box 201, the upper surface of the upper heat exchange fin 204 is tightly connected with the first hot water pipe 202, a phase change material 205 is fixedly installed inside the heat exchange box 201, and the top of the phase change material 205 is matched with the fins on the lower surface of the upper heat exchange fin 204; a lower heat exchange fin 206 is fixedly installed inside the heat exchange box 201, a fin on the upper surface of the lower heat exchange fin 206 is matched with the bottom end of the phase change material 205, and a certain position is reserved in the heat exchange box 201 at the bottom of the lower heat exchange fin 206; the material conveying mechanism 300 comprises a material storage tank 301, a liquid conveying pipe 302, a second water pump 303 and a temperature measuring instrument 304; the material storage tank 301 is fixedly arranged on the upper surface of the mounting mechanism 600, the material storage tank 301 is positioned on the left side of the heat exchange tank 201, the infusion tube 302 is fixedly arranged at the bottom of one side of the material storage tank 301, the infusion tube 302 penetrates through two sides of the heat exchange tank 201 and is in fluid communication with the separating mechanism 400, the infusion tube 302 is positioned in the heat exchange tank 201 and is arranged in a multi-layer bending manner, and the upper surface of the part of the infusion tube 302 positioned in the heat exchange tank 201 is tightly connected with the lower surfaces of the lower heat exchange fins; the second water pump 303 is fixedly arranged on the upper surface of the mounting mechanism 600, the second water pump 303 is connected with the infusion tube 302, and the second water pump 303 is positioned between the liquid storage tank 301 and the heat exchange tank 201; the temperature measuring instrument 304 is fixedly arranged on the upper surface of the mounting mechanism 600, and the temperature measuring instrument 304 is connected with the position of the infusion tube 301 out of the heat exchange box 201; the separation mechanism 400 comprises a centrifuge 401, a cavity 402 and a water outlet 403; the centrifuge 401 is fixedly installed on the upper surface of the installation mechanism 600, the cavity 402 is located inside the centrifuge 401, the water outlet 403 penetrates through the centrifuge 401 and is connected with the cavity 402, and the water outlet 403 is located at the bottom of the cavity 402; the preheating mechanism 500 comprises a second hot water pipe 501, a third valve 502, a third water pump 503, a return pipe 504, a fourth valve 505 and a fourth water pump 506; the water inlet end of the second hot water pipe 501 is connected with the bottom end of one side of the heating box 101, and the water inlet end of the second hot water pipe 501 and the first hot water pipe 202 are positioned on the same side; a third valve 502 is arranged on the second hot water pipe 501, and the third valve 502 is positioned at the water inlet end of the first hot water pipe 501; the water outlet end of the second hot water pipe 501 is connected with the cavity 402, a third water pump 503 is fixedly installed on the upper surface of the centrifuge 401, and the third water pump 503 is connected with the second hot water pipe 501; a water inlet end of the return pipe 504 is connected with the water outlet 403, a water outlet end of the return pipe 504 is connected with a water inlet formed in the upper surface of the heating box 101, a fourth valve 505 is fixedly installed on one side of the centrifuge 401, the fourth valve 505 is connected with the return pipe 504, a fourth water pump 506 is fixedly installed on the upper surface of the installation mechanism 600, and the fourth water pump 506 is connected with the return pipe 504; the mounting mechanism 600 includes a base 601, a non-slip pad 602; the non-slip pad 602 is made of non-slip material, and the non-slip pad 602 is fixedly mounted on the lower surface of the base 601.
The working principle is as follows: before working, enough clean water is added into the heating box 101 to electrify the heating wire 109, the clean water in the heating box 101 is heated, after the clean water is heated to a certain degree, the third valve 502 and the fourth valve 506 are opened, the third water pump 503 is opened to lead the hot water in the heating box 101 to the cavity 402 of the centrifuge 401 to preheat the cavity 402, then the fourth water pump 506 is opened to lead the clean water in the cavity 402 to be pumped into the heating box 101 through the return pipe 504, thereby the clean water can be recycled, after the cavity 402 is preheated, the first water pump 203 is opened to lead the hot water in the heating box 101 to circulate through the first hot water pipe 202, when the hot water passes through the heat exchange box 201, the heat in the first hot water pipe 202 is absorbed by the upper heat exchange fin 204, then the heat is stored in the phase-change material 205, the second water pump 303 is opened to lead the fermentation liquor in the liquid storage box 301 to enter the cavity 402 of the centrifuge 401 through the liquid storage pipe 302, when the fermentation liquid in the liquid conveying pipe 302 passes through the heat exchange box 201, the heat in the phase change material 205 is transferred to the fermentation liquid through the lower heat exchange fins 206, so as to heat the fermentation liquid.
It should be understood that the above examples are only for clarity of illustration and are not intended to limit the embodiments. Other variations and modifications will be apparent to persons skilled in the art in light of the above description. And are neither required nor exhaustive of all embodiments. And obvious variations or modifications are possible which remain within the scope of the appended claims.
Claims (7)
1. The separation device for producing oil from hydrolyzed sugar liquor of walnut endophytic bacteria HB1310 fermented cotton stalks is characterized by comprising a heating mechanism (100), a heat exchange mechanism (200), a material conveying mechanism (300), a separation mechanism (400), a preheating mechanism (500) and an installation mechanism (600);
heating mechanism (100) fixed mounting is directly over heat exchange mechanism (200), just heat exchange mechanism (200) and heating mechanism (100) fluid intercommunication, heat exchange mechanism (200) fixed mounting is at the upper surface of installation mechanism (600), defeated material mechanism (300) sets up the left side at heat exchange mechanism (200), and defeated material mechanism (300) runs through heat exchange mechanism (200) inside setting, separating mechanism (400) set up on heat exchange mechanism (200) right side, separating mechanism (400) and defeated material mechanism (300) fluid intercommunication, just separating mechanism (400) and heating mechanism (100) are through preheating mechanism (500) fluid intercommunication.
2. The walnut endophytic bacterium HB1310 fermented cotton stalk hydrolyzed sugar liquid oil production separation device according to claim 1, wherein the heating mechanism (100) comprises a heating box (101), a support rod (102), a water inlet pipe (103), a first valve (104), a water outlet pipe (105), a second valve (106), an electric box (107), a connecting rod (108) and a heating wire (109);
the heating box (101) is a square box body, the heating box (101) is made of insulating materials, the heating box (101) is fixedly arranged right above the heat exchange mechanism (200) through support rods (102), the number of the support rods (102) is four, and the four support rods (102) are respectively and fixedly arranged at the four corners of the bottom of the heating box (101);
a water inlet pipe (103) is fixedly installed on one side of the heating box (101), the water inlet pipe (103) is located on one side of the heating box (101) close to the top, and a first valve (104) is arranged on the water inlet pipe (103); a water outlet pipe (105) is fixedly installed on the other side of the heating box (101), the water outlet pipe (105) is located at a position, close to the bottom end, of one side of the heating box (101), and a second valve (106) is arranged on the water outlet pipe (105);
an electric box (107) is fixedly mounted at the top of the heating box (101), and the electric box (107) is positioned at the center of the top of the heating box (101); the bottom of the heating box (101) is fixedly provided with two connecting rods (108), the two connecting rods (108) extend into the heating box (101) through the top wall of the heating box (101), and the two connecting rods (108) are symmetrically arranged; two the cavity has all been seted up to the inside of connecting rod (108), two heater strip (109) are all provided with inside the cavity, two heater strip (109) top in the cavity all is connected with electronic box (107), just heater strip (109) interconnect and expose in heating cabinet (101) of two cavity bottoms.
3. The walnut endophytic bacterium HB1310 fermented cotton stalk hydrolyzed sugar liquor oil production separation device according to claim 1, wherein the heat exchange mechanism (200) comprises a heat exchange box (201), a first hot water pipe (202), a first water pump (203), upper heat exchange fins (204), a phase change material (205) and lower heat exchange fins (206);
the heat exchange box (201) is fixedly arranged on the upper surface of the mounting mechanism (600), the heat exchange box (201) is a square box body, and the area of the upper surface of the heat exchange box (201) is equal to that of the lower surface of the heating box (101);
a first hot water pipe (202) is fixedly mounted on the lower surface of the heating box (101), a water inlet of the first hot water pipe (202) is located at a position, close to the right end, of the lower surface of the heating box (101), a water outlet of the first hot water pipe (202) is located at a position, close to the left end, of the lower surface of the heating box (101), the first hot water pipe (202) penetrates through the top wall of the heat exchange box (201) and passes through the interior of the heat exchange box (201), the part, located inside the heat exchange box (201), of the first hot water pipe (202) is in multi-layer bending arrangement, a first water pump (203) is fixedly mounted on the upper surface of the heat exchange box (201), and the first water pump (203) is connected with one end, close to the water inlet, of the first;
an upper heat exchange fin (204) is fixedly installed inside the heat exchange box (201), the upper surface of the upper heat exchange fin (204) is tightly connected with the first hot water pipe (202), a phase change material (205) is fixedly installed inside the heat exchange box (201), and the top of the phase change material (205) is matched with fins on the lower surface of the upper heat exchange fin (204); the heat exchange box is characterized in that lower heat exchange fins (206) are fixedly mounted inside the heat exchange box (201), fins on the upper surfaces of the lower heat exchange fins (206) are matched with the bottom end of the phase change material (205), and a certain position is reserved in the heat exchange box (201) at the bottom of the lower heat exchange fins (206).
4. The walnut endophytic bacterium HB1310 fermented cotton stalk hydrolyzed sugar liquid oil production separation device according to claim 1, wherein the material conveying mechanism (300) comprises a material storage tank (301), a liquid conveying pipe (302), a second water pump (303) and a temperature measuring instrument (304);
the liquid conveying pipe is characterized in that the storage box (301) is fixedly mounted on the upper surface of the mounting mechanism (600), the storage box (301) is located on the left side of the heat exchange box (201), a liquid conveying pipe (302) is fixedly mounted at the bottom of one side of the storage box (301), the liquid conveying pipe (302) penetrates through two sides of the heat exchange box (201) and is communicated with fluid of the separating mechanism (400), the liquid conveying pipe (302) is located inside the heat exchange box (201) and is arranged in a multi-layer bent mode, and the upper surfaces of the parts, located inside the heat exchange box (201), of the liquid conveying pipe (302) are tightly connected with the lower surfaces of the lower heat exchange fins (;
the second water pump (303) is fixedly arranged on the upper surface of the mounting mechanism (600), the second water pump (303) is connected with the infusion tube (302), and the second water pump (303) is positioned between the liquid storage tank (301) and the heat exchange tank (201); the temperature measuring instrument (304) is fixedly arranged on the upper surface of the mounting mechanism (600), and the temperature measuring instrument (304) is connected with the position of the infusion tube (301) out of the heat exchange box (201).
5. The walnut endophytic bacterium HB1310 fermented cotton stalk hydrolyzed sugar liquor oil production separation device according to claim 1, wherein the separation mechanism (400) comprises a centrifuge (401), a cavity (402) and a water outlet (403);
the centrifuge (401) is fixedly installed on the upper surface of the installation mechanism (600), the cavity (402) is located inside the centrifuge (401), the water outlet (403) penetrates through the centrifuge (401) and is connected with the cavity (402), and the water outlet (403) is located at the bottom of the cavity (402).
6. The walnut endophytic bacterium HB1310 fermented cotton stalk hydrolyzed sugar liquid oil production separation device according to claim 1, wherein the preheating mechanism (500) comprises a second hot water pipe (501), a third valve (502), a third water pump (503), a return pipe (504), a fourth valve (505) and a fourth water pump (506);
the water inlet end of the second hot water pipe (501) is connected with the bottom end of one side of the heating box (101), and the water inlet end of the second hot water pipe (501) and the first hot water pipe (202) are located on the same side; a third valve (502) is arranged on the second hot water pipe (501), and the third valve (502) is positioned at the water inlet end of the first hot water pipe (501); the water outlet end of the second hot water pipe (501) is connected with the cavity (402), a third water pump (503) is fixedly mounted on the upper surface of the centrifuge (401), and the third water pump (503) is connected with the second hot water pipe (501);
the water inlet end of the return pipe (504) is connected with the water outlet (403), the water outlet end of the return pipe (504) is connected with the water inlet formed in the upper surface of the heating box (101), a fourth valve (505) is fixedly mounted on one side of the centrifuge (401), the fourth valve (505) is connected with the return pipe (504), a fourth water pump (506) is fixedly mounted on the upper surface of the mounting mechanism (600), and the fourth water pump (506) is connected with the return pipe (504).
7. The walnut endophytic bacterium HB1310 fermented cotton stalk hydrolyzed sugar liquor oil production separation device according to claim 1, wherein the mounting mechanism (600) comprises a base (601), a non-slip mat (602);
the anti-skid pad (602) is made of anti-skid materials, and the anti-skid pad (602) is fixedly mounted on the lower surface of the base (601).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110123096.0A CN112934491B (en) | 2021-01-29 | 2021-01-29 | Separation device for producing oil from walnut endophytic bacterium HB1310 fermentation cotton stalk hydrolysis sugar liquid |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202110123096.0A CN112934491B (en) | 2021-01-29 | 2021-01-29 | Separation device for producing oil from walnut endophytic bacterium HB1310 fermentation cotton stalk hydrolysis sugar liquid |
Publications (2)
Publication Number | Publication Date |
---|---|
CN112934491A true CN112934491A (en) | 2021-06-11 |
CN112934491B CN112934491B (en) | 2022-05-24 |
Family
ID=76239610
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202110123096.0A Active CN112934491B (en) | 2021-01-29 | 2021-01-29 | Separation device for producing oil from walnut endophytic bacterium HB1310 fermentation cotton stalk hydrolysis sugar liquid |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN112934491B (en) |
Citations (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2198750A1 (en) * | 1994-09-01 | 1996-03-07 | Nathan S. Hale | Permanent heat activated transfer printing process and composition |
CN2871510Y (en) * | 2006-03-10 | 2007-02-21 | 李庆权 | Household water distiller |
US20080058192A1 (en) * | 2006-09-05 | 2008-03-06 | Samsung Electronics Co., Ltd. | Centrifugal force based microfluidic device having thermal activation unit, microfluidic system including the same and method of operating the microfluidic system |
CN101280935A (en) * | 2008-05-09 | 2008-10-08 | 清华大学 | Dry-type phase-change thermal storage floor heating terminal device |
GB0919934D0 (en) * | 2009-11-16 | 2009-12-30 | Sunamp Ltd | Energy storage systems |
DE102010004358A1 (en) * | 2010-01-12 | 2011-06-16 | Deutsches Zentrum für Luft- und Raumfahrt e.V. | Latent heat accumulator for use as e.g. overheating protection device in open solar receiver system of solar power station, has cells are made of high temperature-steady material and limit at channel, where fluid flows through channel |
CN102872981A (en) * | 2012-09-10 | 2013-01-16 | 曲险峰 | Method and device for centrifugally separating and removing solid impurities in investment casting pattern material at high speed |
CN203422007U (en) * | 2013-03-21 | 2014-02-05 | 中益能(北京)技术有限公司 | Integrated pipeline-type phase-changing heat storage module |
CN103884102A (en) * | 2012-12-22 | 2014-06-25 | 张娜 | Heating set |
CN105983550A (en) * | 2016-06-17 | 2016-10-05 | 宿迁淮海科技服务有限公司 | Efficient tea leaf producing and washing device |
CN106578207A (en) * | 2016-11-17 | 2017-04-26 | 贵州省凤冈县永田露茶业有限公司 | Tea leaf coarse filtration extraction apparatus |
CN106890474A (en) * | 2017-02-07 | 2017-06-27 | 合山锌业科技有限公司 | Residual neat recovering system |
CN108531207A (en) * | 2018-06-19 | 2018-09-14 | 大庆高新区百世环保科技开发有限公司 | A kind of oily sludge substance treating method and its device using conduction oil indirectly heat |
CN208303036U (en) * | 2018-04-10 | 2019-01-01 | 杭州普优生物技术有限公司 | A kind of workbench with pre-add heat function centrifuge |
CN208332414U (en) * | 2018-05-31 | 2019-01-04 | 安阳优创电器有限责任公司 | A kind of heating heat exchange box of phase-transition heat-storage |
CN209597443U (en) * | 2019-01-14 | 2019-11-08 | 乌拉特中旗毅腾矿业有限责任公司 | A kind of block cleaned coal centrifuge |
WO2020057834A1 (en) * | 2018-09-19 | 2020-03-26 | Arcelik Anonim Sirketi | A rotary heat exchanger |
CN210663590U (en) * | 2019-09-29 | 2020-06-02 | 上海奉坤新材料有限公司 | Centrifugal hot-blast surge bin |
CN111271989A (en) * | 2020-02-26 | 2020-06-12 | 袁一军 | Heat exchange structure with symmetrical characteristics, heat exchanger with heat exchange structure and application method |
CN211430969U (en) * | 2019-11-14 | 2020-09-08 | 黄山荷琇生物科技有限公司 | Pine needle hydrolat preparation system |
-
2021
- 2021-01-29 CN CN202110123096.0A patent/CN112934491B/en active Active
Patent Citations (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA2198750A1 (en) * | 1994-09-01 | 1996-03-07 | Nathan S. Hale | Permanent heat activated transfer printing process and composition |
CN2871510Y (en) * | 2006-03-10 | 2007-02-21 | 李庆权 | Household water distiller |
US20080058192A1 (en) * | 2006-09-05 | 2008-03-06 | Samsung Electronics Co., Ltd. | Centrifugal force based microfluidic device having thermal activation unit, microfluidic system including the same and method of operating the microfluidic system |
CN101280935A (en) * | 2008-05-09 | 2008-10-08 | 清华大学 | Dry-type phase-change thermal storage floor heating terminal device |
GB0919934D0 (en) * | 2009-11-16 | 2009-12-30 | Sunamp Ltd | Energy storage systems |
DE102010004358A1 (en) * | 2010-01-12 | 2011-06-16 | Deutsches Zentrum für Luft- und Raumfahrt e.V. | Latent heat accumulator for use as e.g. overheating protection device in open solar receiver system of solar power station, has cells are made of high temperature-steady material and limit at channel, where fluid flows through channel |
CN102872981A (en) * | 2012-09-10 | 2013-01-16 | 曲险峰 | Method and device for centrifugally separating and removing solid impurities in investment casting pattern material at high speed |
CN103884102A (en) * | 2012-12-22 | 2014-06-25 | 张娜 | Heating set |
CN203422007U (en) * | 2013-03-21 | 2014-02-05 | 中益能(北京)技术有限公司 | Integrated pipeline-type phase-changing heat storage module |
CN105983550A (en) * | 2016-06-17 | 2016-10-05 | 宿迁淮海科技服务有限公司 | Efficient tea leaf producing and washing device |
CN106578207A (en) * | 2016-11-17 | 2017-04-26 | 贵州省凤冈县永田露茶业有限公司 | Tea leaf coarse filtration extraction apparatus |
CN106890474A (en) * | 2017-02-07 | 2017-06-27 | 合山锌业科技有限公司 | Residual neat recovering system |
CN208303036U (en) * | 2018-04-10 | 2019-01-01 | 杭州普优生物技术有限公司 | A kind of workbench with pre-add heat function centrifuge |
CN208332414U (en) * | 2018-05-31 | 2019-01-04 | 安阳优创电器有限责任公司 | A kind of heating heat exchange box of phase-transition heat-storage |
CN108531207A (en) * | 2018-06-19 | 2018-09-14 | 大庆高新区百世环保科技开发有限公司 | A kind of oily sludge substance treating method and its device using conduction oil indirectly heat |
WO2020057834A1 (en) * | 2018-09-19 | 2020-03-26 | Arcelik Anonim Sirketi | A rotary heat exchanger |
CN209597443U (en) * | 2019-01-14 | 2019-11-08 | 乌拉特中旗毅腾矿业有限责任公司 | A kind of block cleaned coal centrifuge |
CN210663590U (en) * | 2019-09-29 | 2020-06-02 | 上海奉坤新材料有限公司 | Centrifugal hot-blast surge bin |
CN211430969U (en) * | 2019-11-14 | 2020-09-08 | 黄山荷琇生物科技有限公司 | Pine needle hydrolat preparation system |
CN111271989A (en) * | 2020-02-26 | 2020-06-12 | 袁一军 | Heat exchange structure with symmetrical characteristics, heat exchanger with heat exchange structure and application method |
Also Published As
Publication number | Publication date |
---|---|
CN112934491B (en) | 2022-05-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN112934491B (en) | Separation device for producing oil from walnut endophytic bacterium HB1310 fermentation cotton stalk hydrolysis sugar liquid | |
CN102363360A (en) | High overflow type drawing hot water tank | |
CN111729346A (en) | Distillation plant for chemical industry pharmacy | |
CN217527370U (en) | High stability syrup mixing apparatus | |
CN211546438U (en) | High-efficient vacuum degassing refining kettle | |
CN207918802U (en) | A kind of termite low temperature stirring enzymolysis equipment | |
CN215103158U (en) | A distillation plant for rice wine production | |
CN220389693U (en) | Die cutting machine for label production | |
CN208542088U (en) | A kind of medical treatment internal medicine medication purification agitating device | |
CN201397822Y (en) | Manual etching cleaning machine with pre-heating | |
CN214562735U (en) | Water type mold temperature controller for injection mold | |
CN209739795U (en) | heat-preservation glue tray | |
CN218232428U (en) | Enzyme decomposition reaction kettle for processing tremella polysaccharide extracting solution | |
CN212247070U (en) | Enzyme reactor device | |
CN200966546Y (en) | Steamer convenient for adding water | |
CN214026950U (en) | Injection mold with quick cooling structure | |
CN214076100U (en) | Heat exchange type saccharification jar | |
CN219482729U (en) | Electric heating constant temperature water bath kettle convenient for changing water liquid | |
CN221526874U (en) | Heating structure for producing desulfurization catalyst | |
CN215540796U (en) | Reation kettle is used in single-ended structure vinyl silicone oil preparation | |
CN221145629U (en) | Water outlet pipe structure and have its thermos | |
CN214636279U (en) | Temperature adjusting device in plate tower | |
CN221133474U (en) | Syrup retort cleaning device | |
CN219603540U (en) | Efficient dewatering system | |
CN217323923U (en) | Temperature control device for preparing oligosaccharide |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
GR01 | Patent grant | ||
GR01 | Patent grant |