Conditioning and/or heating plant and process of controlling the same plant

• US 10,443,862 B2
• Filed: 09/09/2016
• Issued: 10/15/2019
• Est. Priority Date: 09/09/2015
• Status: Active Grant

• Current Assignee: Fimcim S.P.A.
• Original Assignee: Fimcim S.P.A.
• Inventors: Guidetti, Tiziano, Chiarello, Andrea, Cerutti, Alfredo, Cimberio, Roberto, Cimberio, Renzo
• Primary Examiner(s): Jonaitis, Justin M
• Application Number:
  US15/260,833
• Publication Number:
  US 20170067656A1
• Time in Patent Office: 1,131 Days
• Field of Search: 165208, 165200, 165201, 165205, 165212
• CPC Class Codes: F16K 37/00 Special means in or on valves or other cut-off apparatus for indicating or recording operation thereof, or for enabling an alarm to be given
• CPC Class Codes: F16K 37/0041 for measuring valve parameters F16K37/0033 takes precedence
• CPC Class Codes: F16K 37/005 for measuring fluid parameters F16K37/0033 takes precedence
• CPC Class Codes: F16K 5/04 with plugs having cylindrical surfaces; Packings therefor
• CPC Class Codes: F24D 10/00 District heating systems
• CPC Class Codes: F24D 19/1012 by regulating the speed of a pump
• CPC Class Codes: F24D 19/1015 using a valve or valves
• CPC Class Codes: F24D 19/1036 Having differential pressure measurement facilities
• CPC Class Codes: F24D 19/1048 Counting of energy consumption
• CPC Class Codes: F24D 2220/0264 Hydraulic balancing valves
• CPC Class Codes: F24D 2220/0271 Valves
• CPC Class Codes: F24D 2220/0292 Fluid distribution networks
• CPC Class Codes: F24D 2220/042 Temperature sensors
• CPC Class Codes: F24D 2220/044 Flow sensors
• CPC Class Codes: F24D 2220/046 Pressure sensors
• CPC Class Codes: F24D 3/02 with forced circulation, e.g. by pumps pump constructions F04
• CPC Class Codes: F24D 3/10 Feed-line arrangements, e.g. providing for heat-accumulator tanks, expansion tanks ; Hydraulic components of a central heating system
• CPC Class Codes: F24F 11/83 by controlling the supply of heat-exchange fluids to heat-exchangers
• CPC Class Codes: F24F 11/84 using valves
• CPC Class Codes: F24F 11/85 using variable-flow pumps
• CPC Class Codes: G05D 23/1924 : using thermal energy, the availability of which is aleatory
• CPC Class Codes: G05D 23/1928 : sensing the temperature of one space
• CPC Class Codes: G05D 7/0635 : by action on throttling means G05D7/0688, G05D7/0694 take precedence
• CPC Class Codes: Y02B 30/17 : District heating
• CPC Class Codes: Y02B 30/70 : Efficient control or regulation technologies, e.g. for control of refrigerant flow, motor or heating

Abstract

A conditioning or heating plant and a process of controlling the plant, wherein plant comprises at least one circuit for distributing a carrier fluid, having a delivery line, a return line, and a plurality of channels directly or indirectly connected to the delivery line and return line and configured for supplying respective environments to be conditioned and/or heated, at least one heat treatment central group placed on the circuit. The plant has, for each of the channels, at least one respective heat exchange unit and at least one flow-rate regulator.

Claims

1. A process of controlling a conditioning and/or heating plant, said plant being of a type comprising:

at least one circuit configured for distributing a carrier fluid, having;

at least one delivery line of the carrier fluid,

at least one return line of the carrier fluid, and

a plurality of channels directly or indirectly connected to said delivery line and return line and configured for supplying said carrier fluid to respective environments to be conditioned and/or heated,

at least one heat treatment central group placed on the circuit,

wherein for each of said channels, the plant further comprises;

at least one respective heat exchange unit operating on each of said channels and configured for supplying a respective environment to be conditioned and/or heated,

at least one flow-rate regulator operating on each of said channels and configured for regulating a flow-rate of a carrier fluid passing through the respective heat exchange unit, wherein each flow-rate regulator comprises at least one valve having a valve body exhibiting at least one inlet, at least one outlet connected by at least one passage which puts in fluid communication the inlet with the outlet, and at least one fluid intercepting element operating in said passage, said fluid intercepting element defining, cooperatively with the valve body, a fluid passage opening having a size variable as a function of positions taken by the fluid intercepting element in relation to the valve body,

wherein said controlling process comprises;

commanding the heat treatment central group to regulate at least one general parameter, the at least one general parameter selected from the group consisting of;

the hydraulic head imposed to the carrier fluid passing through the heat treatment central group,

the heating imposed to the carrier fluid passing through the heat treatment central group,

the cooling imposed to the carrier fluid passing through the heat treatment central group, and

the flow-rate imposed to the carrier fluid on the delivery line,

commanding the flow-rate regulator on each of said channels to impose a respective desired value of an operative parameter in relation to each channel where the respective flow-rate regulator is present, and

executing a hydraulic optimization cycle, the hydraulic optimization cycle comprising at least the following steps;

commanding the heat treatment central group for reducing the value of said general parameter,

controlling each flow-rate regulator by increasing the size of said fluid passage opening,

verifying if—

following the step of controlling each flow-rate regulator—

the plant has reached a desired hydraulic efficiency condition where the passage opening of one or more flow-rate regulators exhibits a maximum opening, and

following the verifying step, if it is determined that the plant has reached the desired hydraulic efficiency condition, interrupting the hydraulic optimization cycle.

2. The process according to claim 1, wherein:

commanding the heat treatment central group for reducing the value of said general parameter and to maintain the desired value of the respective operative parameter occurs after controlling each flow-rate regulator for increasing the size of said fluid passage opening.

3. The process according to claim 1, wherein:

controlling each flow-rate regulator by increasing the size of said passage opening for maintaining the desired value of the respective operative parameter occurs after commanding the heat treatment central group to reduce the value of said general parameter.

4. The process according to claim 1, wherein said operative parameter is:

a flow parameter in each channel selected from the group consisting of;

a flow-rate passing through each flow-rate regulator,

a pressure difference between a first section of the channel upstream of each said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator, and

a pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel downstream of the calibrated orifice, the calibrated orifice being placed on each channel, upstream of each said flow-rate regulator.

5. The process according to claim 4, wherein commanding the flow-rate regulator is based on the deviation between the desired value and a measured value of the respective operative parameter.

6. The process according to claim 5, wherein said measured value of the respective operative parameter is collected by at least one hydraulic sensor selected from the group consisting of:

a flowmeter configured for detecting the flow rate passing through the flow-rate regulator,

a pressure differential sensor configured for detecting the pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator,

a pressure differential sensor configured for detecting the pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator,

a system of two distinct pressure sensors configured for enabling to calculate the pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator, and

a system of two distinct pressure sensors configured for enabling to calculate the pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator.

7. The process according to claim 6, further comprising determining the measured value of the operative parameter based on the detection performed by the hydraulic sensor.

8. The process according to claim 1, wherein the process comprises:

determining, by a position sensor and for each flow rate regulator, the positions taken by the intercepting element, along a predetermined operative stroke in relation to the valve body, and transmitting a respective signal by the position sensor, wherein the intercepting element is configured for taking a plurality of positions along said operative stroke corresponding to different opening degrees of said passage opening and wherein said position sensor is configured for emitting a signal at each step of a predetermined amount performed by the intercepting element along the operative stroke.

9. The process according to claim 8,

wherein verifying if the plant has reached the desired hydraulic efficiency condition comprises:

receiving the signal of said position sensor relating to each of said flow-rate regulators,

verifying, based on said signal of the position sensor, an opening state of the intercepting element of each of said valves,

determining when the passage opening of a predetermined number of said valves reaches a condition of maximum opening of the passage opening, and

establishing that the desired hydraulic efficiency condition has been reached when one or more of said valves reach the maximum opening condition of the respective passage opening.

10. The process according to claim 1, wherein the heat treatment central group comprises:

at least one pump, and

at least one unit selected between a heating unit and a refrigerating unit,

and wherein reducing the value of the general parameter during the hydraulic optimization cycle comprises;

commanding the pump for reducing the hydraulic head across the heat treatment central group if the general parameter is the hydraulic head imposed to the carrier fluid passing through the heat treatment central group,

commanding the pump for maintaining unchanged the overall flow-rate of the fluid in the delivery line if the general parameter is the flow-rate imposed to the carrier fluid on the delivery line,

commanding the heating unit to reduce the temperature of the delivering and/or returning carrier fluid if the general parameter is the cooling imposed to the carrier fluid passing through the heat treatment central group;

or

commanding the refrigerating unit to increase the temperature of the carrier fluid in the delivery and/or return line if the general parameter is the heating imposed to the carrier fluid passing through the heat treatment central group.

11. The process according to claim 1, wherein said optimization cycle further comprises:

if it is verified that the plant has reached the desired hydraulic efficiency, comparing, for each of said channels, said desired value of the operative parameter with said effective value of the same parameter,

verifying, for each of said channels, if the effective value of the operative parameter deviates more than a predetermined threshold from the desired value of the same parameter, —

if, as a result of said comparing step, it results that for a number of channels the effective value of the operative parameter deviates more than a predetermined threshold of the desired value of the same parameter, controlling the heat treatment central group for changing at least one general parameter and reducing the deviation between the effective value of the operative parameter and the desired value of the same parameter, and

repeating the preceding three steps until, for each heat exchange unit, the effective value of the operative parameter does not deviate more than a predetermined threshold from the desired value of the same parameter.

12. The process according to claim 1, wherein said operative parameter is an energy parameter relating to the heat exchange unit associated to the respective flow-rate regulator, said energy parameter being selected from the group consisting of:

the thermal power released from the carrier fluid passing through each heat exchange unit,

the thermal power received from the carrier fluid passing through each heat exchange unit,

the heat released by the carrier fluid in a predetermined time interval when passes through each heat exchange unit, and

the heat absorbed by the carrier fluid in a predetermined time interval when passes through each heat exchange unit.

13. The process according to claim 12, wherein said process further comprises:

detecting, with at least one thermal sensor, a measured value of a thermal parameter dependent on the temperature difference between a first section of each channel upstream of said heat exchange unit and a second section of each channel downstream of the same heat exchange unit,

wherein the thermal sensor is selected from the group consisting of;

a first thermal detector configured for detecting the temperature in a first section of each channel upstream of said heat exchange unit and a second thermal detector configured for detecting the temperature in a second section of each channel downstream of the same heat exchange unit, and

a differential thermal sensor connected to the first section of each channel upstream of said thermal exchange unit and to the second section of each channel downstream of the same heat exchange unit and configured for detecting the temperature difference between said first and second sections of each channel.

14. The process according to claim 12, further comprising commanding the flow-rate regulator based on the deviation between a desired value and a measured value of the respective operative parameter.

15. The process according to claim 14, wherein said plant comprises at least one hydraulic sensor selected from the group consisting of:

a flowmeter configured for detecting the flow rate passing through the flow-rate regulator,

a pressure differential sensor configured for detecting a pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator,

a pressure differential sensor configured for detecting a pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator,

a system of two distinct pressure sensors configured for enabling to calculate a pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator, and

a system of two distinct pressure sensors configured for enabling to calculate a pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator;

and wherein the process comprises determining the measured value of the operative parameter based on the detection performed by the hydraulic sensor and a thermal sensor.

16. The process of claim 1 wherein, if it is determined that the plant has not reached the desired hydraulic efficiency condition, the hydraulic optimization cycle is repeated.

17. A conditioning and/or heating plant comprising:

at least one circuit, of distributing a carrier fluid, having;

at least one delivery line of the carrier fluid,

at least one return line of the carrier fluid, and

a plurality of channels directly or indirectly connected to said delivery line and said return line, and configured for supplying the carrier fluid to respective environments to be conditioned and/or heated,

at least one heat treatment central group placed on the circuit,

for each of said channels, the plant further comprising;

at least one respective heat exchange unit operating on each of said channels and configured for supplying a respective environment to be conditioned and/or heated,

at least one flow-rate regulator operating on each of said channels, configured for regulating a flow rate of a carrier fluid passing through the respective heat exchange unit, wherein each flow-rate regulator comprises at least one valve having a valve body exhibiting at least one inlet, at least one outlet connected by at least one passage which puts in fluid communication the inlet with the outlet, and at least one fluid intercepting element operating in said passage, said fluid intercepting element defining, cooperatively with the valve body, a fluid passage opening having a width variable as a function of positions taken by the fluid intercepting element in relation to the valve body,

at least one control device communicatively connected to and active on each flow-rate regulator and on said heat treatment central group, the control device being configured for executing a controlling process which comprises;

commanding the heat treatment central group to regulate at least one general parameter selected from the group consisting of;

the hydraulic head imposed to the carrier fluid passing through the heat treatment central group,

the heating imposed to the carrier fluid passing through the heat treatment central group,

the cooling imposed to the carrier fluid passing through the heat treatment central group, and

the flow-rate imposed to the carrier fluid on the delivery line,

commanding the flow-rate regulator on each of said channels to impose a respective desired value of an operative parameter in relation to each channel where the respective flow-rate regulator is present, and

executing a hydraulic optimization cycle comprising;

commanding the heat treatment central group for reducing the value of said general parameter,

controlling each flow-rate regulator by increasing the size of said fluid passage opening;

verifying if—

following the step of controlling each flow-rate regulator—

the plant has reached a desired hydraulic efficiency condition where the passage opening of one or more flow-rate regulators exhibits a maximum opening, and

following the verifying step, if it is determined that the plant has reached the desired hydraulic efficiency condition, interrupting the hydraulic optimization cycle.

18. The plant according to claim 17, wherein said operative parameter is a flow parameter in each channel, the flow parameter being selected from the group consisting of:

a flow-rate passing through each flow-rate regulator,

a pressure difference between a first section of the channel upstream each said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator, and

a pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel downstream of the calibrated orifice, the calibrated orifice being placed on each channel, upstream of each said flow-rate regulator;

wherein said plant comprises at least one hydraulic sensor configured for measuring the flow parameter, the at least one hydraulic sensor being selected from the group consisting of;

a flowmeter configured for detecting the flow rate passing through the flow-rate regulator,

a pressure differential sensor configured for detecting the pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator,

a pressure differential sensor configured for detecting the pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator,

a system of two distinct pressure sensors configured for enabling to calculate the pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator, and

a system of two distinct pressure sensors configured for enabling to calculate the pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator,

wherein imposing a respective desired value of an operative parameter relating to each flow-rate regulator comprises commanding the flow-rate regulator based on the deviation between a desired value and a measured value of the respective operative parameter, with the measured value of the operative parameter being determined based on the detection performed by the hydraulic sensor.

19. The plant according to claim 17, wherein the plant comprises, for each flow-rate regulator, a position sensor configured for determining the positions taken by the intercepting element, along a predetermined operative stroke in relation to the valve body, and for transmitting a respective signal, wherein the intercepting element is configured for taking a plurality of positions along said operative stroke corresponding to different opening degrees of said passage opening and wherein said position sensor is configured for emitting a signal at each step of a predetermined amount performed by the intercepting element along the operative stroke;

and wherein verifying if the plant has reached a desired hydraulic efficiency condition comprises;

receiving the signal of said position sensor relating to each of said flow-rate regulators,

verifying, based on said signal of the position sensor, an opening state of the intercepting element of each of said valves,

determining when the passage opening of a predetermined number of said valves reaches a condition of maximum opening of the passage opening, and

establishing that the desired hydraulic efficiency condition has been reached when one or more of said valves reach the maximum opening condition of the respective passage opening.

20. The plant according to claim 17, wherein the heat treatment central group comprises:

at least one pump, and

at least one unit selected between a heating unit and a refrigerating unit,

and wherein reducing the value of the general parameter during the hydraulic optimization cycle comprises;

commanding the pump for reducing the hydraulic head across the heat treatment central group if the general parameter is the hydraulic head imposed to the carrier fluid passing through the heat treatment central group,

commanding the pump for maintaining unchanged the overall flow-rate of the fluid in the delivery line if the general parameter is the flow-rate imposed to the carrier fluid on the delivery line,

commanding the heating unit to reduce the temperature of the delivering and/or returning carrier fluid if the general parameter is the cooling imposed to the carrier fluid passing through the heat treatment central group, or

commanding the refrigerating unit to increase the temperature of the carrier fluid in the deliver and/or return line if the general parameter is the heating imposed to the carrier fluid passing through the heat treatment central group.

21. The plant according to claim 17, wherein said optimization cycle further comprises:

if it is verified that the plant has reached the desired hydraulic efficiency, comparing, for each of said channels, said desired value of the operative parameter with said effective value of the same parameter,

verifying, for each of said channels, if the effective value of the operative parameter deviates more than a predetermined threshold from the desired value of the same parameter,

if, as a result of said comparing step, it results that for a number of channels the effective value of the operative parameter deviates more than a predetermined threshold of the desired value of the same parameter, controlling the heat treatment central group for changing at least one general parameter and reducing the deviation between the effective value of the operative parameter and the desired value of the same parameter, and

repeating the preceding three steps until, for each heat exchange unit, the effective value of the operative parameter does not deviate more than a predetermined threshold from the desired value of the same parameter.

22. The plant according to claim 17, wherein said operative parameter is an energy parameter relating to the heat exchange unit associated to the respective flow-rate regulator, said energy parameter being selected from the group consisting of:

the thermal power released from the carrier fluid passing through each heat exchange unit,

the thermal power received from the carrier fluid passing through each heat exchange unit,

the heat released by the carrier fluid in a predetermined time interval when passes through each heat exchange unit, and

the heat absorbed by the carrier fluid in a predetermined time interval when passes through each heat exchange unit;

wherein said plant comprises at least one thermal sensor configured for detecting a measured value of a thermal parameter dependent on the temperature difference between a first section of each channel upstream of said heat exchange unit and a second section of each channel downstream of the same heat exchange unit,

wherein the thermal sensor is selected between;

a first thermal detector configured for detecting the temperature in a first section of each channel upstream of said heat exchange unit and a second thermal detector configured for detecting the temperature in a second section of each channel downstream of the same heat exchange unit, and

a differential thermal sensor connected to the first section of each channel upstream of said thermal exchange unit and to the second section of each channel downstream of the same heat exchange unit and configured for detecting the temperature difference between said first and second sections of each channel,

wherein said plant comprises at least one hydraulic sensor selected from the group consisting of;

a flowmeter configured for detecting the flow rate passing through the flow-rate regulator,

a pressure differential sensor configured for detecting a pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator,

a pressure differential sensor configured for detecting a pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator,

a system of two distinct pressure sensors configured for enabling to calculate a pressure difference between a first section of the channel upstream of said flow-rate regulator and a second section of the same channel downstream of the same flow-rate regulator, and

a system of two distinct pressure sensors configured for enabling to calculate a pressure difference between a first section of a channel upstream of a calibrated orifice and a second section of the same channel placed downstream of the calibrated orifice, the calibrated orifice being upstream of the flow-rate regulator;

wherein imposing a respective desired value of an operative parameter relating to each flow-rate regulator provides to command the flow-rate regulator based on the deviation between a desired value and a measured value of the respective operative parameter,

and wherein determining the measured value of the operative parameter is based on the detection performed by the hydraulic sensor and thermal sensor.

23. The process of claim 17 wherein, if it is determined that the plant has not reached the desired hydraulic efficiency condition, the hydraulic optimization cycle is repeated.