CN212226716U - Liquid wax production line - Google Patents

Liquid wax production line Download PDF

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Publication number
CN212226716U
CN212226716U CN202020206184.8U CN202020206184U CN212226716U CN 212226716 U CN212226716 U CN 212226716U CN 202020206184 U CN202020206184 U CN 202020206184U CN 212226716 U CN212226716 U CN 212226716U
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pipeline
liquid wax
valve
wax
tank
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CN202020206184.8U
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朱卫民
王绘宏
王传真
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Inner Mongolia Xihe Chemical Co ltd
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Inner Mongolia Xihe Chemical Co ltd
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Abstract

The utility model discloses a liquid wax production line, including adding the wax melting tank of solid wax, the first pipeline that one end and wax melting tank are connected, install the first valve on first pipeline, the measurement cauldron that top one side is connected with the first pipeline other end, one end and measurement cauldron top opposite side fixed connection's second pipeline, install the second valve on the second pipeline, the liquid wax metering tank that the bottom is connected with the second pipeline other end, the third pipeline that one end is connected on top of the liquid wax metering tank, the liquid wax storage tank that bottom and the third pipeline other end are connected, install on the third pipeline and be close to the third valve on liquid wax metering tank top, install on the third pipeline and be close to the fourth valve of liquid wax storage tank bottom to and the business turn over material device of being connected with the liquid wax storage tank. The utility model discloses add and melt the wax jar, drop into solid wax and melt in the wax jar, make the solid wax after melting flow into the measurement cauldron through first pipeline in, the sealed problem of measurement cauldron has been solved to this structure.

Description

Liquid wax production line
Technical Field
The utility model relates to a paraffin processing equipment field, specific saying relates to a liquid wax production line.
Background
The liquid wax is also called paraffin oil, colorless, odorless, tasteless and non-fluorescent oily liquid, and is obtained by distilling heavy oil under reduced pressure. Mixtures of n-alkanes having melting points below 40 ℃ from C10 to C18, which are petroleum products. The mixture composed of various normal alkanes with melting point below 40 ℃ and ranging from C10 to C18 is mainly used as a raw material for producing chlorinated paraffin, and can also be used as a detergent raw material, cosmetics, daily necessities diluent, solvent and the like.
In the process of preparing the liquid wax, a manhole cover needs to be thoroughly opened, then the solid wax is poured into a metering kettle, and finally the manhole cover is covered, so that the process can relate to the sealing problem of the metering kettle, and the produced liquid wax is easy to fail to reach the standard; the liquid wax in the liquid wax metering tank is guided into the metering kettle through the pump, and is easy to solidify in winter with low temperature, so that a pipeline is blocked, a liquid wax production line is caused to have problems, and the production of the liquid wax is delayed.
SUMMERY OF THE UTILITY MODEL
For overcoming the problem that prior art exists, the utility model provides a do not influence the difficult liquid wax production line that blocks up the pipeline of measurement cauldron leakproofness, liquid wax.
In order to achieve the above object, the utility model adopts the following technical scheme:
a liquid wax production line comprises a wax melting tank for adding solid wax, a first pipeline with one end connected with the wax melting tank, a first valve arranged on the first pipeline, a metering kettle with one side of the top connected with the other end of the first pipeline, a second pipeline with one end fixedly connected with the other side of the top of the metering kettle, a second valve arranged on the second pipeline, a liquid wax metering tank with the bottom connected with the other end of the second pipeline, a third pipeline with one end connected with the top end of the liquid wax metering tank, a liquid wax storage tank with the bottom connected with the other end of the third pipeline, a third valve arranged on the third pipeline and close to the top end of the liquid wax metering tank, and a fourth valve arranged on the third pipeline and close to the bottom of the liquid wax storage tank, and the feeding and discharging device is connected with the liquid wax storage tank, wherein the liquid wax metering tank is higher than the metering kettle.
Further, melt the wax jar including the jar body that is used for loading solid wax, set up in on the jar body and be used for leading-in solid wax's entry, with entry articulated shutter, install in the internal steam coil of jar, and install in on the jar body and be used for driving the internal solid wax that melts of jar and flow into the submerged pump in the first pipeline, wherein, first pipeline penetrates in the jar body.
Further, the measurement cauldron includes the cauldron body that top both sides are connected with first pipeline, second pipeline respectively, sets up in manhole on the cauldron body, with manhole articulated manhole cover is used for supporting the cauldron body supporting leg of the cauldron body sets up in the blowoff hole of cauldron body bottom one side, with discharging pipe that cauldron body bottom opposite side is connected, and install in fifth valve on the discharging pipe, wherein, liquid wax metering tank is located the position and is higher than the cauldron body and locate the position.
Further, the feeding and discharging device comprises a fourth pipeline penetrating into the side wall of the liquid wax storage tank and extending into the bottom of the liquid wax storage tank, a tenth valve and a sixth valve which are adjacently installed on the fourth pipeline, a fifth pipeline connected with the fourth pipeline and positioned between the tenth valve and the sixth valve, a sixth pipeline with one end connected with the bottom end of the liquid wax storage tank, a seventh valve and a ninth valve which are adjacently installed on the sixth pipeline, a liquid wax pump connected with the other end of the sixth pipeline, a seventh pipeline connected with the sixth pipeline and positioned between the ninth valve and the liquid wax pump, and an eighth valve arranged on the seventh pipeline, wherein the fifth pipeline is connected with the sixth pipeline at a position between the seventh pipeline and the liquid wax pump, the seventh valve is located on a sixth pipeline close to the bottom end of the liquid wax storage tank, and the ninth valve is located on a sixth pipeline far away from the bottom end of the liquid wax storage tank.
When the utility model is used, solid wax is added into the wax melting tank firstly, and is heated through the steam coil pipe to be melted into liquid state, the first valve is opened, and meanwhile, the submerged pump is used for providing power, so that the melted solid wax flows into the first pipeline and further flows into the metering kettle; based on the fact that a mixture consisting of various normal paraffins with the melting point of below 40 ℃ and the melting point of C10 to C18 is needed for preparing the chlorinated paraffin, liquid waxes with different molecular structures in the liquid wax storage tank need to be prepared, the third valve and the fourth valve are opened, the liquid wax in the liquid wax storage tank flows into the liquid wax metering tank through the third pipeline, the second valve is opened, the liquid wax in the liquid wax metering tank flows into the metering kettle to be mixed with melted solid wax, the mixed liquid wax is mixed into the liquid wax capable of being used for preparing the chlorinated paraffin, the fifth valve is opened, the mixed liquid wax is led out through the discharge pipe and is conveyed to an external chlorinated paraffin reaction tower to react; when the liquid wax in the liquid wax storage tank needs to be used, the seventh valve, the ninth valve and the sixth valve can be opened, and the liquid wax pump is started, so that the liquid wax in the liquid wax storage tank flows through the sixth pipeline, the fifth pipeline and the fourth pipeline and finally flows out; when the liquid wax taken out from the liquid wax storage tank is residual, the tank truck loaded with the liquid wax can be connected with the seventh pipeline, the eighth valve, the ninth valve and the fifth valve are opened simultaneously, and the residual liquid wax flows through the seventh pipeline, the sixth pipeline, the fifth pipeline and the fourth pipeline by the power in the tank truck and finally enters the liquid wax storage tank.
Compared with the prior art, the utility model discloses following beneficial effect has:
(1) the utility model discloses an add and melt the wax jar, make it melt through steam coil pipe in dropping into the wax jar of melting with solid wax to in providing power through the submerged pump and making the solid wax after melting through first pipeline inflow measurement cauldron, the sealed problem of measurement cauldron has been solved to this structure.
(2) The utility model discloses a submerged pump provides power for first pipeline for the internal liquid wax flow direction of jar first pipeline, the solid wax after melting in constantly gushing into first pipeline forms certain impact force to first pipeline, can avoid first pipeline to be blockked up.
(3) The utility model discloses a make liquid wax metering tank position higher than the measurement cauldron position to make second pipeline both ends be connected with measurement cauldron top and liquid wax metering tank bottom respectively, make the liquid wax that is located the liquid wax metering tank utilize the siphon principle to get into the measurement cauldron in, avoided remaining liquid wax in the second pipeline, and then make the second pipeline block up after avoiding liquid wax to solidify.
(4) The utility model discloses a pass through the third pipe connection bottom the liquid wax storage tank with liquid wax metering tank top, and because the liquid wax in the liquid wax storage tank is bulky, based on the pressure effect of liquid wax, make the liquid wax in the liquid wax storage tank export to the third pipeline, and then in the input liquid wax metering tank, and the liquid wax in the liquid wax metering tank is because in the siphon principle constantly flows to the measurement cauldron, make the liquid wax metering tank produce certain suction to the liquid wax in the third pipeline, residual liquid wax in the third pipeline has been avoided, and then make the third pipeline block up after avoiding the liquid wax to solidify.
(5) The utility model discloses a feeding and discharging device is when the feeding, and the power that the usable liquid wax that comes from the tank car injection produced, and liquid wax flows into seventh pipeline, sixth pipeline, fifth pipeline and fourth pipeline from the tank car, flows into the liquid wax storage tank at last, provides certain impact to seventh pipeline, sixth pipeline, fifth pipeline and fourth pipeline in proper order, can avoid seventh pipeline, sixth pipeline, fifth pipeline and fourth pipeline to block up; when the ejection of compact, can extract the liquid wax in the liquid wax storage tank through the power that the liquid wax pump produced for the liquid wax flows through the sixth pipeline, fifth pipeline and fourth pipeline, flows the device of input and output material at last, goes to the workshop, provides certain impact to sixth pipeline, fifth pipeline and fourth pipeline in proper order, can avoid the sixth pipeline, fifth pipeline and fourth pipeline to block up, can make the pipeline of input and output material device be difficult for blockking up, can not influence the use of input and output material device.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic view of a partial structure of the part a of the present invention.
Fig. 3 is a schematic partial structure diagram of part B of the present invention.
Wherein, the names corresponding to the reference numbers are:
1-a wax melting tank, 2-a first pipeline, 3-a first valve, 4-a metering kettle, 5-a second pipeline, 6-a second valve, 7-a liquid wax metering tank, 8-a third pipeline, 9-a liquid wax storage tank, 10-a third valve, 11-a fourth valve, 12-a feeding and discharging device, 13-a tank body, 14-an inlet, 15-a baffle door, 16-a steam coil, 17-a submerged pump, 18-a tank body, 19-a manhole, 20-a manhole cover, 21-a tank body supporting leg, 22-a sewage discharge hole, 23-a discharge pipe, 24-a fifth valve, 25-a fourth pipeline, 26-a tenth valve, 27-a sixth valve, 28-a fifth pipeline, 29-a sixth pipeline and 30-a seventh valve, 31-liquid wax pump, 32-eighth valve, 33-ninth valve, 34-seventh pipeline.
Detailed Description
The present invention will be further described with reference to the following description and examples, which include but are not limited to the following examples.
Examples
As shown in fig. 1 to 3, the liquid wax production line includes a wax melting tank 1, a first pipeline 2, a first valve 3, a metering kettle 4, a second pipeline 5, a second valve 6, a liquid wax metering tank 7, a third pipeline 8, a liquid wax storage tank 9, a third valve 10, a fourth valve 11, a feeding and discharging device 12, a tank body 13, an inlet 14, a baffle door 15, a steam coil 16, a submerged pump 17, a kettle body 18, a manhole 19, a manhole cover 20, kettle body supporting legs 21, a sewage discharge hole 22, a discharge pipe 23, a fifth valve 24, a fourth pipeline 25, a tenth valve 26, a sixth valve 27, a fifth pipeline 28, a sixth pipeline 29, a seventh valve 30, a liquid wax pump 31, an eighth valve 32, a ninth valve 33, and a seventh pipeline 34. The wax melting tank 1 is used for adding and melting solid wax and comprises a tank body 13 for loading the solid wax, an inlet 14 which is formed in the tank body 13 and used for introducing the solid wax, a stop door 15 which is hinged with the inlet 14, a steam coil pipe 16 which is arranged in the tank body 13 and used for heating the solid wax, and a submerged pump 17 which is arranged on the tank body 13 and used for driving the solid wax melted in the tank body 13 to flow into the first pipeline 2; one end of the first pipeline 2 penetrates into the tank body 13 and extends into the bottom of the tank body 13, and the first pipeline is connected and matched with the submerged pump 17 and is used for pumping the melted solid wax in the tank body 13; the first valve 3 is arranged on the first pipeline 2 and used for controlling the on-off of the first pipeline 2; one side of the top end of the metering kettle 4 is connected with the other end of the first pipeline 2 and is used for receiving liquid wax from a liquid wax storage tank 9 flowing in from the first pipeline 2 and flowing in from the second pipeline 5, the metering kettle comprises a kettle body 18, a manhole 19, a manhole cover 20, kettle body supporting legs 21, a sewage discharge hole 22, a discharge pipe 23 and a fifth valve 24, wherein the kettle body 18 is connected with the first pipeline 2 and the second pipeline 5 respectively at the two sides of the top and is used for loading a wax body formed by mixing melted solid wax and the liquid wax from the liquid wax storage tank 9, the manhole 19 is arranged on the kettle body 18, the manhole cover 20 is hinged with the manhole 19, the kettle body supporting legs 21 are used for supporting the kettle body 18, the sewage discharge hole 22 is arranged on one side of the bottom of the kettle body 18; one end of the second pipeline 5 is connected with the top of the kettle body 18, and the other end of the second pipeline is connected with the bottom of the liquid wax metering tank 7, so that the liquid wax in the liquid wax metering tank 7 can completely flow into the kettle body 18; the second valve 6 is arranged on the second pipeline 5 and used for controlling the on-off of the second pipeline 5; the bottom of the liquid wax metering tank 7 is connected with the second pipeline 5, the top end of the liquid wax metering tank is connected with the third pipeline 8, and the liquid wax metering tank is used for metering liquid wax input into the kettle body 18 and is positioned higher than the metering kettle 4; one end of a third pipeline 8 is connected with the top end of the liquid wax metering tank 7, and the other end of the third pipeline is connected with the bottom of the liquid wax storage tank 9; the third valve 10 is arranged on one side of the third pipeline 8 close to the top end of the liquid wax metering tank 7 and is used for controlling the input quantity of the liquid wax metering tank 7; the fourth valve 11 is arranged on one side of the third pipeline 8 close to the bottom of the liquid wax storage tank 9 and used for controlling the output quantity of the liquid wax storage tank 9; the liquid wax storage tank 9 is used for storing liquid wax consisting of alkane; the feeding and discharging device 12 is connected with the liquid wax storage tank 9 and is used for inputting or outputting the liquid wax in the liquid wax storage tank 9, which comprises a fourth pipeline 25 penetrating into the side wall of the liquid wax storage tank 9 and extending into the bottom of the liquid wax storage tank 9, a tenth valve 26 and a sixth valve 27 adjacently installed on the fourth pipeline 25, a fifth pipeline 28 connected with the fourth pipeline 25 and located between the tenth valve 26 and the sixth valve 27, a sixth pipeline 29 connected with the bottom end of the liquid wax storage tank 9 and connected with the fifth pipeline 28 at one end, the sixth pipeline 29 and the fifth pipeline 28 connected between a seventh pipeline 34 and a liquid wax pump 31, a seventh valve 30 installed on the sixth pipeline 29, a liquid wax pump 31 connected with the other end of the sixth pipeline 29, a seventh pipe 34 connected to the sixth pipe 29 and located between the seventh valve 30 and the liquid wax pump 31, and an eighth valve 32 installed on the seventh pipe 34.
When the utility model is used, solid wax is added into the wax melting tank firstly, and is heated through the steam coil pipe to be melted into liquid state, the first valve is opened, and meanwhile, the submerged pump is used for providing power, so that the melted solid wax flows into the first pipeline and further flows into the metering kettle; based on the fact that a mixture consisting of various normal paraffins with the melting point of below 40 ℃ and the melting point of C10 to C18 is needed for preparing the chlorinated paraffin, liquid waxes with different molecular structures in the liquid wax storage tank need to be prepared, the third valve and the fourth valve are opened, the liquid wax in the liquid wax storage tank flows into the liquid wax metering tank through the third pipeline, the second valve is opened, the liquid wax in the liquid wax metering tank flows into the metering kettle to be mixed with melted solid wax, the mixed liquid wax is mixed into the liquid wax capable of being used for preparing the chlorinated paraffin, the fifth valve is opened, the mixed liquid wax is led out through the discharge pipe and is conveyed to an external chlorinated paraffin reaction tower to react; when the liquid wax in the liquid wax storage tank needs to be used, the seventh valve, the ninth valve and the sixth valve can be opened, and the liquid wax pump is started, so that the liquid wax in the liquid wax storage tank flows through the sixth pipeline, the fifth pipeline and the fourth pipeline and finally flows out; when the liquid wax taken out from the liquid wax storage tank is residual, the tank truck loaded with the liquid wax can be connected with the seventh pipeline, the eighth valve, the ninth valve and the fifth valve are opened simultaneously, and the residual liquid wax flows through the seventh pipeline, the sixth pipeline, the fifth pipeline and the fourth pipeline by the power in the tank truck and finally enters the liquid wax storage tank.
The above embodiment is only one of the preferred embodiments of the present invention, and should not be used to limit the protection scope of the present invention, but all the insubstantial changes or modifications made in the spirit and the idea of the main design of the present invention, the technical problems solved by the embodiment are still consistent with the present invention, and all should be included in the protection scope of the present invention.

Claims (4)

1. The liquid wax production line is characterized by comprising a wax melting tank (1) for adding solid wax, a first pipeline (2) with one end connected with the wax melting tank (1), a first valve (3) arranged on the first pipeline (2), a metering kettle (4) with one side of the top connected with the other end of the first pipeline (2), a second pipeline (5) with one end fixedly connected with the other side of the top of the metering kettle (4), a second valve (6) arranged on the second pipeline (5), a liquid wax metering tank (7) with the bottom connected with the other end of the second pipeline (5), a third pipeline (8) with one end connected with the top end of the liquid wax metering tank (7), a liquid wax storage tank (9) with the bottom connected with the other end of the third pipeline (8), and a third valve (10) which is arranged on the third pipeline (8) and is close to the top end of the liquid wax metering tank (7), the fourth valve (11) is arranged on the third pipeline (8) and is close to the bottom of the liquid wax storage tank (9), and the feeding and discharging device (12) is connected with the liquid wax storage tank (9), wherein the liquid wax metering tank (7) is higher than the metering kettle (4).
2. The liquid wax production line according to claim 1, wherein the wax melting tank (1) comprises a tank body (13) for loading solid wax, an inlet (14) which is arranged on the tank body (13) and used for introducing the solid wax, a stop door (15) which is hinged with the inlet (14), a steam coil (16) which is arranged in the tank body (13), and a submerged pump (17) which is arranged on the tank body (13) and used for driving the solid wax melted in the tank body (13) to flow into the first pipeline (2), wherein the first pipeline (2) penetrates into the tank body (13).
3. The liquid wax production line according to claim 1, wherein the metering kettle (4) comprises a kettle body (18) with two top sides connected with the first pipeline (2) and the second pipeline (5) respectively, a manhole (19) arranged on the kettle body (18), a manhole cover (20) hinged with the manhole (19), kettle body supporting legs (21) used for supporting the kettle body (18), a sewage discharge hole (22) arranged on one side of the bottom of the kettle body (18), a discharge pipe (23) connected with the other side of the bottom of the kettle body (18), and a fifth valve (24) arranged on the discharge pipe (23), wherein the liquid wax metering tank (7) is higher than the kettle body (18).
4. A liquid wax production line according to claim 1, wherein the feeding and discharging device (12) comprises a fourth pipe (25) penetrating into the side wall of the liquid wax storage tank (9) and penetrating into the bottom of the liquid wax storage tank (9), a tenth valve (26) and a sixth valve (27) mounted adjacent to the fourth pipe (25), a fifth pipe (28) connected to the fourth pipe (25) and located between the tenth valve (26) and the sixth valve (27), a sixth pipe (29) connected at one end to the bottom end of the liquid wax storage tank (9), a seventh valve (30) and a ninth valve (33) mounted adjacent to the sixth pipe (29), a liquid wax pump (31) connected to the other end of the sixth pipe (29), a seventh pipe (34) connected to the sixth pipe (29) and located between the ninth valve (33) and the liquid wax pump (31), and an eighth valve (32) installed on the seventh pipeline (34), wherein the fifth pipeline (28) is connected with the sixth pipeline (29) and the connection position is between the seventh pipeline (34) and the liquid wax pump (31), the seventh valve (30) is located on the sixth pipeline (29) close to the bottom end of the liquid wax storage tank (9), and the ninth valve (33) is located on the sixth pipeline (29) far away from the bottom end of the liquid wax storage tank (9).
CN202020206184.8U 2020-02-25 2020-02-25 Liquid wax production line Active CN212226716U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020206184.8U CN212226716U (en) 2020-02-25 2020-02-25 Liquid wax production line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202020206184.8U CN212226716U (en) 2020-02-25 2020-02-25 Liquid wax production line

Publications (1)

Publication Number Publication Date
CN212226716U true CN212226716U (en) 2020-12-25

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ID=73912670

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202020206184.8U Active CN212226716U (en) 2020-02-25 2020-02-25 Liquid wax production line

Country Status (1)

Country Link
CN (1) CN212226716U (en)

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