Greawan Farming, Plant 2 - Executive Summary

| Accident History | Chemicals | Emergency Response | Registration | Source | Executive Summary |

Risk & Process Safety Management Program 
 
 
 
Executive Summary 
 
for 
 
Gerawan Farming 
1467 E. Dinuba Ave. 
Reedley, CA 93654 
(559) 787-8780 
FAX (559) 637-1662 
 
 
June 21, 1999 
 
 
 
 
 
 
 
 
 
 
Prepared by: 
 
Solutions Environmental Health & Safety, Inc. 
6687 N. Blackstone Avenue, Suite 103 
Fresno, California 93710 
(559) 435-4244 
FAX (559) 435-8503 
www.SEHS-Inc.com 
 
 
Table of Contents For Executive Summary 
 
1.   THE GERAWAN FARMING - PLANT 2, RISK & PROCESS SAFETY MANAGEMENT PROGRAM   1 
2. DESCRIPTION OF AMMONIA SYSTEM   1 
3. AMMONIA RELEASE SCENARIOS   2 
3.1 WORST CASE SCENARIO   2 
3.2 ALTERNATIVE CASE SCENARIO   2 
4. GENERAL ACCIDENT RELEASE & AMMONIA SPECIFIC PREVENTION STEPS   2 
5. FIVE YEAR ACCIDENT HISTORY   3 
6. EMERGENCY ACTION PLAN   3 
7. PLANNED CHANGES TO IMPROVE SAFETY 3 
 
 
1.   GERAWAN FARMING FACILITIES RISK & PROCESS SAFETY MANAGEMENT PROGRAMS 
This is to inform all interested persons, including employees, that Gerawan Farming is preparing unified Risk & Process Safety Management Progr 
ams to comply with California's Accidental Release Prevention (CalARP) Program (in California CCR Title 19, Chapter 4.5, Program Level 3 Elements, and Federally Title 40 CFR Part 68) and California OSHA's "Process Safety Management (PSM) of Acutely Hazardous Materials" standard (in California CCR Title 8, Section 5189, "Process Safety Management of Acutely Hazardous Materials" and Federally Title 29 Code of Federal Regulations (CFR) 1910.119).  This program is being prepared to address the risks involved with the presence of anhydrous ammonia in an amount in excess of 10,000 lbs which is contained in refrigeration systems located at our #2 plant: 
 
Gerawan Farming, Plant 2 
1467 E. Dinuba Ave. 
Reedley, CA 93654 
 
Our program will promote overall plant, worker, and public safety. The program will enable our facility to prevent the occurrence, and minimize the consequences, of significant releases of anhydrous ammonia. Overall, the program is designed to prevent accidental fatalities, injur 
ies and illnesses and avoid physical property damage. 
 
Our company has an exemplary safety record, one that we are quite proud of.  Our program incorporates and brings together several existing safety programs which already set forth rules, procedures and practices which help our employees protect themselves and our neighbors. 
2. DESCRIPTION OF AMMONIA SYSTEM 
We operate three commercial packinghouses for deciduous tree fruit - apricots, nectarines, peaches, plums, and  
 
grapes.  All of our facilities have ammonia systems that provide refrigeration capacity to multiple cold rooms equipped with forced air cooling for cooling fruit.  In addition, we have cold rooms where palleted product is stored.   
 
All of our systems operate in a similar manner.  High pressure liquid from our main receiver is piped to each cold room, where it passes through an expansion valve into a low temperature & pressure accumulator vessel.  Cold liquid ammonia from the accumulator is piped to evaporator coils.  A 
s heat is absorbed from the produce, the liquid in the evaporator coils vaporizes.  Low temperature and pressure gas from the coils is returned to the accumulator vessel.  A suction return line carries the vapor to our engine room, where it passes through a compressor.  The high pressure discharge from the compressor is sent to a water cooled condenser where the high pressure gas ammonia is liquified and returned to our receiver. 

 
Plant 2 has two engine rooms with a total system charge of 189,000 lbs.  The two ammonia systems are independent and are not connected through piping. 
 
3. AMMONIA RELEASE SCENARIOS 
3.1 Worst Case Scenario 
We have estimated the offsite impact for a worst case scenario release for each of our three plants. In our opinion, it is extremely unlikely that the worst-case scenario will ever take place.  Our receiver meets industry standards for manufacture and quality control of pressure vessels; ammonia is not corrosive in this service; pressure safety relief valv 
es limit the operating pressure in this vessel; and our operators are trained in the safe operation of our system. 
 
Gerawan Farming, Plant 2 
Our worst case scenario is the failure of a high pressure receiver containing 96,000 lbs of ammonia.  The receiver is located inside our engine room.  Therefore, if this release were to take place, the release would be passively mitigated.  The release would take place over a ten minute period.  Using the EPA program RMP*Comp we estimated the ammonia would travel 4.0 miles (rural conditions) before dispersing enough to no longer pose a hazard to the public.  A map showing the area that would be affected is attached. 
 
 
3.2 Alternative Case Scenario 
All of our plants are equipped with safety relief valves that vent to the atmosphere.  For all three of our plants, our most likely alternative release scenario is as follows.  A high pressure safety relief valve lifts and fails to reseat.  The rated release rate for our high pressure safety relief valve 
is 125 lbs/min.  We assume the leak would continue for 10 minutes until the header pipe was switched over to the backup safety relieve valve. Following industry practice, our relief valves are installed in pairs with a switch over valve, and the discharge is piped to a release point that is remote from the valve. Under this scenario 1,250 lbs of ammonia would be released over a time period of 10 minutes.  Using RMP*Comp we estimate that the ammonia would travel 0.3 miles (rural conditions) before dispersing enough to no longer pose a hazard to the public. A map showing the areas that would be affected at each of our plants is attached. 
4. GENERAL ACCIDENT RELEASE & AMMONIA SPECIFIC PREVENTION STEPS 
The ammonia refrigeration system at Gerawan Farming is an integral part of the overall business. It is extremely important that it is maintained and operated in a safe and efficient manner.  Management is committed to making sure that all employees are made aware of the potential danger of  
an ammonia leak. 
 
 
 
The ammonia refrigeration system/process is constantly being monitored by our refrigeration engineer, Ray Penner.  In addition, the system/process is checked frequently by our outside refrigeration contractor, California Controlled Atmosphere, who also performs an annual pre-season preventative maintenance review of our system/process equipment.   The system/process is controlled by a computer which monitors many process variables, and allows remote control.  In the event of a system upset the computer actuates a dialing program that alerts key personnel and responders.  We have ammonia detectors which also trigger alerts.  The detectors are inspected monthly and serviced annually.  
 
 
Our ammonia refrigeration system was designed and built by professional refrigeration engineers in accordance with ANSI/IIAR 2-1992 "Standard for Equipment, Design, and Installation of Ammonia Mechanical Refrigerating Systems."  It was also built in compliance with the Uniform Building 
Code and Uniform Mechanical Code applicable at the time of construction. 
 
Our ammonia refrigeration system is equipped with safety relief valves.  These valves limit the operating pressures of the entire system, and prevent failures due to overpressurization. 
5. FIVE YEAR ACCIDENT HISTORY 
Gerawan Farming has not had any reportable accidents within the last five years. 
6. EMERGENCY ACTION PLAN 
This facility's emergency response program is based on the Cal OSHA requirements for Emergency Action Plans (in California CCR Title 8, Section 3220, "Emergency Action Plans" and Federally Title 29 CFR 1910.38 and 1910.119) and HAZWOPER (standard (in California CCR Title 8, Section 5192, "Hazardous Waste Operations and Emergency Response" and Federally Title 29 CFR 1910.120).  
 
Strategically, we will respond Defensively to a release.  Under this plan our employees will take whatever steps are necessary to bring a release under control. Initial training to the defensive level (First Responder, Ope 
rations Level) as defined in the HAZWOPER regulations will take place before the end of the year.  The first priority will be to operate the ammonia system to bring a release under control safely, from a distance, without donning personal protective equipment.  Steps might include stopping the flow of ammonia to a leak point, or using the compressor to suck ammonia away from a leak point. Further response requiring the donning of personal protective equipment would be done by an outside agency.  All response activities would be coordinated with the local fire department and the Fresno County Fire Department Hazardous Materials Response Team. 
7. PLANNED CHANGES TO IMPROVE SAFETY 
As of June 21, 1999, the time that this Executive Summary is being submitted, our Risk & Process Safety Management Plan is not complete.  The reason is that in order to do it right a lot of work must be done.  We simply do not have enough qualified employees or resources to meet the initial deadline. Our company 
operates seasonally and we have found that our ability to allocate managerial and operator resources to prepare this plan depends upon our workload.  In addition, we have found it necessary to obtain help from outside vendors for some critical elements, such as preparing Piping & Instrumentation Diagrams and conducting a Process Hazard Analysis.  These vendors are attempting to meet the requests of numerous facilities such as ours at the same time, and have the same problem of only a limited number of people qualified to carry out the required tasks.  Thus, these vendors are setting completion dates for plan elements that we cannot entirely control. 
 
However, we have prepared the following milestones and allotted times for the completion of our plan: 
 
 
MilestoneAllotted Time 
* Conduct Offsite Consequence Analysis - Done 
* Prepare RMP*Submit showing status as of 6/21/99 - Done 
* Collect Process Safety Information 30 days - By Aug 1, 1999 
* Conduct Process Hazard Analysis On or around A 
ug 1, 1999 
* Finish PHA documentation including Action List 30 days - By Nov 1, 1999 
* Prepare Process Prevention Program elements 90 days - By Oct 1, 1999 
* Prepare Standard Operating Procedures 90 days - By Oct 1, 1999 
* Compile all elements into Risk & Process Safety  
Management Program, review internally, and submit 120 days - By Nov 1, 1999 
 
 
 
We understand our obligations to consolidate our safety activities in a Risk Management Program under the CalARP regulation.  We are committed to preparing and implementing a Risk & Process Safety Management Program according to the above milestone and timeline chart. 
Gerawan Farming Risk & Process Safety Management Program
Click to return to beginning