System and method to prevent the oxidizer overheating using cold side bypass for a VOCs treatment system with series rotor

A method for preventing an oxidizer overheating using cold side bypass for a volatile organic compounds (VOCs) treatment system with a series rotor used in an organic waste air treatment system, comprising:

• providing a thermal oxidizer (TO), a first heat exchanger, a second heat exchanger, a third heat exchanger, a first cold-side transporting pipeline, a first adsorption rotor, a second adsorption rotor, and a chimney,
• wherein the thermal oxidizer (TO) is equipped with a burner and a chamber, the burner and the chamber are linked together, the thermal oxidizer (TO) is equipped with an entrance and an exit, the entrance is installed in the burner, the exit is installed in the chamber, the first heat exchanger is equipped with a first cold-side pipeline and a first hot-side pipeline, the second heat exchanger is equipped with the second cold-side pipeline and a second hot-side pipeline, and the third heat exchanger is equipped with a third cold-side pipeline and a third hot-side pipeline,
• wherein a first end of the first cold-side transporting pipeline is connected with an end of the first cold-side pipeline, and a second end of the first cold-side transporting pipeline is connected with the entrance of the thermal oxidizer (TO),
• wherein the first adsorption rotor is equipped with an adsorption zone, a cooling zone, and a desorption zone, the first adsorption rotor is connected with an exhaust air intake pipeline, a first purified air discharge pipeline, a first cooling air intake pipeline, a first cooling air transporting pipeline, a first hot air transporting pipeline, and a first desorption-treated air pipeline, and the second adsorption rotor is equipped with the adsorption zone, the cooling zone and the desorption zone,
• wherein the second adsorption rotor is connected with a second purified air discharge pipeline, a second cooling air intake pipeline, a second cooling air transporting pipeline, a second hot air transporting pipeline, and a second desorption-treated air pipeline;
• sending the waste air to a first side of the adsorption zone in the first adsorption rotor via the exhaust air intake pipeline;
• after adsorption at the adsorption zone of the first adsorption rotor, outputting the adsorbed air to the adsorption zone of the second adsorption rotor from a second side of the adsorption zone in the first adsorption rotor through an end of the first purified air discharge pipeline;
• transporting the cooling air to the cooling zone of the first adsorption rotor through an end of the first cooling air intake pipeline to perform cooling, then, transporting the cooling air that has passed through the cooling zone of the first adsorption rotor to a first end of the third cold-side pipeline in the third heat exchanger through the end of the first cooling air transporting pipeline;
• transporting the hotter air to the desorption zone of the first adsorption rotor through the first hot air transporting pipeline that is connected to a second end of the third cold-side pipeline in the third heat exchanger to perform desorption, then, through an end of the first desorption-treated air pipeline, transporting the desorption-treated air to one end of the first cold-side pipeline in the first heat exchanger;
• transporting the desorption-treated air to a first end of a fourth cold-side pipeline in a fourth heat exchanger via the first cold-side transporting pipeline which is connected at the end of the first cold-side pipeline in the first heat exchanger, then, transporting the desorption-treated air to the entrance of the thermal oxidizer (TO) via the fourth cold-side transporting pipeline which is connected to a second end of the fourth cold-side pipeline through the fourth heat exchanger as incinerated air;
• transporting the incinerated air at the burner of the thermal oxidizer (TO) to a first end of the fourth hot-side pipeline in the fourth heat exchanger, then, transporting the incinerated air to a first end of the third hot-side pipeline in the third heat exchanger through a second end of the fourth hot-side pipeline in the fourth heat exchanger, next, transporting the incinerated air to a first end of the second hot-side pipeline in the second heat exchanger through a second end of the third hot-side pipeline in the third heat exchanger, then, transporting it to a first end of the first hot-side pipeline in the first heat exchanger through a second end of the second hot-side pipeline in the second heat exchanger, finally, transporting the incinerated air to the exit of the thermal oxidizer (TO) through a second end of the first hot-side pipeline in the first heat exchanger;
• transporting the adsorbed air in the first purified air discharge pipeline to one side of the adsorption zone in the second adsorption rotor to perform secondary adsorption, then, transporting the secondary adsorbed air to the chimney and discharging the secondary adsorbed air therein via the second purified air discharge pipeline;
• transporting the cooling air to the cooling zone of the second adsorption rotor to perform cooling through an end of the second cooling air intake pipeline, then, transporting the cooling air to a first end of the second cold-side pipeline in the second heat exchanger through an end of the second cooling air transporting pipeline that is passing through the cooling zone of the second adsorption rotor;
• transporting the hotter air to the desorption zone of the second adsorption rotor to perform desorption via the second hot air transporting pipeline which is connected to a second end of the second cold-side pipeline in the second heat exchanger, then outputting the hotter air through an end of the second desorption-treated air pipeline;
• and
• equipping a cold-side proportional damper between the first desorption-treated air pipeline and the first cold-side transporting pipeline, and using the cold-side proportional damper to control airflow of the first desorption-treated air pipeline and the first cold-side transporting pipeline.

A method for preventing an oxidizer overheating using cold side bypass for a volatile organic compounds (VOCs) treatment system with a series rotor for use in an organic waste air treatment system, comprising:

• providing a thermal oxidizer (TO), a first heat exchanger, a second heat exchanger, a third heat exchanger, a first cold-side transporting pipeline, a first adsorption rotor, a second adsorption rotor and a chimney,
• wherein the thermal oxidizer (TO) is equipped with a burner and a chamber, the burner and the chamber are linked together, the thermal oxidizer (TO) is equipped with an entrance and an exit, the entrance is installed in the burner, the exit is installed in the chamber, the first heat exchanger is equipped with a first cold-side pipeline and a first hot-side pipeline, the second heat exchanger is equipped with a second cold-side pipeline and a second hot-side pipeline, and a third heat exchanger is equipped with a third cold-side pipeline and a third hot-side pipeline,
• wherein a first end of the first cold-side transporting pipeline is connected with an end of the first cold-side pipeline, and a second end of the first cold-side transporting pipeline is connected with the entrance of the thermal oxidizer (TO),
• wherein the first adsorption rotor is equipped with an adsorption zone, a cooling zone, and a desorption zone, the first adsorption rotor is connected with an exhaust air intake pipeline, a first purified air discharge pipeline, a first cooling air intake pipeline, a first cooling air transporting pipeline, a first hot air transporting pipeline and a first desorption-treated air pipeline, the second adsorption rotor is equipped with the adsorption zone, and the cooling zone and the desorption zone,
• wherein the second adsorption rotor is connected with a second purified air discharge pipeline, a second cooling air intake pipeline, a second cooling air transporting pipeline, a second hot air transporting pipeline, and a second desorption-treated air pipeline;
• sending the waste air to a first side of the adsorption zone in the first adsorption rotor via the exhaust air intake pipeline;
• after adsorption at the adsorption zone of the first adsorption rotor, outputting the adsorbed air to the adsorption zone of the second adsorption rotor from a second side of the adsorption zone in the first adsorption rotor through an end of the first purified air discharge pipeline;
• transporting the cooling air to the cooling zone of the first adsorption rotor through an end of the first cooling air intake pipeline to perform cooling, then, transporting the cooling air that has passed through the cooling zone of the first adsorption rotor to a first end of the third cold-side pipeline in the third heat exchanger through the end of the first cooling air transporting pipeline;
• transporting the hotter air to the desorption zone of the first adsorption rotor via the first hot air transporting pipeline that is connected to a second end of the third cold-side pipeline in the third heat exchanger to perform desorption, then, through an end of the first desorption-treated air pipeline, transporting the desorption-treated air to one end of the first cold-side pipeline in the first heat exchanger;
• transporting the desorption-treated air to the entrance of the thermal oxidizer (TO) via the first cold-side transporting pipeline which is connected at the end of the first cold-side pipeline in the first heat exchanger as incinerated air;
• transporting the incinerated air at the burner of the thermal oxidizer (TO) to a first end of the third hot-side pipeline in the third heat exchanger, then, transporting the incinerated air to a first end of the second hot-side pipeline in the second heat exchanger through a second end of the third hot-side pipeline in the third heat exchanger, next, transporting the incinerated air to a first end of the first hot-side pipeline in the first heat exchanger through a second end of the second hot-side pipeline in the second heat exchanger, finally, transporting the incinerated air to the exit of the thermal oxidizer (TO) through a second end of the first hot-side pipeline in the first heat exchanger;
• transporting the adsorbed air in the first purified air discharge pipeline to one side of the adsorption zone in the second adsorption rotor to perform secondary adsorption, then, transporting the secondary adsorbed air to the chimney and discharging the secondary adsorbed air therein through the second purified air discharge pipeline;
• transporting the cooling air to the cooling zone of the second adsorption rotor to perform cooling through an end of the second cooling air intake pipeline, then, transporting the cooling air to a first end of the second cold-side pipeline in the second heat exchanger through an end of the second cooling air transporting pipeline that is passing through the cooling zone of the second adsorption rotor;
• transporting the hotter air to the desorption zone of the second adsorption rotor to perform desorption via the second hot air transporting pipeline which is connected to a second end of the second cold-side pipeline in the second heat exchanger, then, outputting the hotter air through an end of the second desorption-treated air pipeline;
• and
• equipping a cold-side proportional damper at the first desorption-treated air pipeline, wherein an end of the cold-side proportional damper allows external air to access, and using the cold-side proportional damper to control airflow of the first desorption-treated air pipeline.

A method for preventing an oxidizer overheating using cold side bypass for a volatile organic compounds (VOCs) treatment system with a series rotor for use in an organic waste air treatment system, comprising:

• providing a thermal oxidizer (TO), a first heat exchanger, a second heat exchanger, a third heat exchanger, a first cold-side transporting pipeline, a first adsorption rotor, a second adsorption rotor, and a chimney,
• wherein the thermal oxidizer (TO) is equipped with a burner and a chamber, the burner and the chamber are linked together, the thermal oxidizer (TO) is equipped with an entrance and an exit, the entrance is installed in the burner, the exit is installed in the chamber, the first heat exchanger is equipped with a first cold-side pipeline and a first hot-side pipeline, the second heat exchanger is equipped with a second cold-side pipeline and a second hot-side pipeline, and the third heat exchanger is equipped with a third cold-side pipeline and a third hot-side pipeline,
• wherein a first end of the first cold-side transporting pipeline is connected to a first end of the first cold-side pipeline, and a second end of the first cold-side transporting pipeline is connected with the entrance of the thermal oxidizer (TO),
• wherein the first adsorption rotor is equipped with an adsorption zone, a cooling zone, and a desorption zone, the first adsorption rotor is connected with an exhaust air intake pipeline, a first purified air discharge pipeline, a first cooling air intake pipeline, a first cooling air transporting pipeline, a first hot air transporting pipeline, and a first desorption-treated air pipeline, and the second adsorption rotor is equipped with the adsorption zone, the cooling zone, and the desorption zone,
• wherein the second adsorption rotor is connected with a second purified air discharge pipeline, a second cooling air intake pipeline, a second cooling air transporting pipeline, a second hot air transporting pipeline, and a second desorption-treated air pipeline;
• sending the waste air to a first side of the adsorption zone in the first adsorption rotor via the exhaust air intake pipeline;
• after adsorption at the adsorption zone of the first adsorption rotor, outputting the adsorbed air to the adsorption zone of the second adsorption rotor from a second side of the adsorption zone in the first adsorption rotor through an end of the first purified air discharge pipeline;
• transporting the cooling air to the cooling zone of the first adsorption rotor through an end of the first cooling air intake pipeline to perform cooling, then, transporting the cooling air that has passed through the cooling zone of the first adsorption rotor to a first end of the third cold-side pipeline in the third heat exchanger through the end of the first cooling air transporting pipeline;
• transporting the hotter air to the desorption zone of the first adsorption rotor via the first hot air transporting pipeline that is connected with a second end of the third cold-side pipeline in the third heat exchanger to perform desorption, then, through an end of the first desorption-treated air pipeline, transporting the desorption-treated air to one end of the first cold-side pipeline in the first heat exchanger;
• transporting the desorption-treated air to the entrance of the thermal oxidizer (TO) through the first cold-side transporting pipeline which is connected to a second end of the first cold-side pipeline in the first heat exchanger as incinerated air;
• transporting the incinerated air at the burner of the thermal oxidizer (TO) to a first end of the first hot-side pipeline in the first heat exchanger, then, transporting the incinerated air to a first end of the third hot-side pipeline in the third heat exchanger through a second end of the first hot-side pipeline in the first heat exchanger, next, transporting the incinerated air to a first end of the second hot-side pipeline in the second heat exchanger through a second end of the third hot-side pipeline in the third heat exchanger, then, transporting it to the second end of the second hot-side pipeline in the second heat exchanger through the second end of the third hot-side pipeline in the third heat exchanger, finally, transporting the incinerated air to the exit of the thermal oxidizer (TO) through the second end of the first hot-side pipeline in the first heat exchanger;
• transporting the adsorbed air in the first purified air discharge pipeline to one side of the adsorption zone in the second adsorption rotor to perform secondary adsorption, then, transporting the secondary adsorbed air to the chimney and discharging the secondary adsorbed air therein via the second purified air discharge pipeline;
• transporting the cooling air to the cooling zone of the second adsorption rotor to perform cooling through an end of the second cooling air intake pipeline, then, transporting the cooling air to a first end of the second cold-side pipeline in the second heat exchanger through an end of the second cooling air transporting pipeline that is passing through the cooling zone of the second adsorption rotor;
• transporting the hotter air to the desorption zone of the second adsorption rotor to perform desorption via the second hot air transporting pipeline which is connected to a second end of the second cold-side pipeline in the second heat exchanger, then outputting the hotter air through an end of the second desorption-treated air pipeline;
• and
• equipping a cold-side proportional damper in the first desorption-treated air pipeline, and using the cold-side proportional damper to control airflow of the first desorption-treated air pipeline.